US7971809B2 - Fibrous materials and composites - Google Patents
Fibrous materials and composites Download PDFInfo
- Publication number
- US7971809B2 US7971809B2 US11/859,325 US85932507A US7971809B2 US 7971809 B2 US7971809 B2 US 7971809B2 US 85932507 A US85932507 A US 85932507A US 7971809 B2 US7971809 B2 US 7971809B2
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- US
- United States
- Prior art keywords
- fibrous material
- less
- percent
- fibrous
- screen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related, expires
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- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H13/00—Other non-woven fabrics
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
- C08L97/02—Lignocellulosic material, e.g. wood, straw or bagasse
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/90—Fillers or reinforcements, e.g. fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/90—Fillers or reinforcements, e.g. fibres
- B29B7/905—Fillers or reinforcements, e.g. fibres with means for pretreatment of the charges or fibres
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- B—PERFORMING OPERATIONS; TRANSPORTING
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- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/88—Adding charges, i.e. additives
- B29B7/90—Fillers or reinforcements, e.g. fibres
- B29B7/92—Wood chips or wood fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/04—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising reinforcements only, e.g. self-reinforcing plastics
- B29C70/06—Fibrous reinforcements only
- B29C70/10—Fibrous reinforcements only characterised by the structure of fibrous reinforcements, e.g. hollow fibres
- B29C70/12—Fibrous reinforcements only characterised by the structure of fibrous reinforcements, e.g. hollow fibres using fibres of short length, e.g. in the form of a mat
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
- C08J5/045—Reinforcing macromolecular compounds with loose or coherent fibrous material with vegetable or animal fibrous material
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
- C08J5/04—Reinforcing macromolecular compounds with loose or coherent fibrous material
- C08J5/10—Reinforcing macromolecular compounds with loose or coherent fibrous material characterised by the additives used in the polymer mixture
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/02—Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
- C10L5/34—Other details of the shaped fuels, e.g. briquettes
- C10L5/36—Shape
- C10L5/363—Pellets or granulates
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
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- D04H1/00—Non-woven fabrics formed wholly or mainly of staple fibres or like relatively short fibres
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M13/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M14/00—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials
- D06M14/02—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin
- D06M14/04—Graft polymerisation of monomers containing carbon-to-carbon unsaturated bonds on to fibres, threads, yarns, fabrics, or fibrous goods made from such materials on to materials of natural origin of vegetal origin, e.g. cellulose or derivatives thereof
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/01—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with natural macromolecular compounds or derivatives thereof
- D06M15/03—Polysaccharides or derivatives thereof
- D06M15/05—Cellulose or derivatives thereof
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M15/00—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment
- D06M15/19—Treating fibres, threads, yarns, fabrics, or fibrous goods made from such materials, with macromolecular compounds; Such treatment combined with mechanical treatment with synthetic macromolecular compounds
- D06M15/21—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D06M15/327—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds of unsaturated alcohols or esters thereof
- D06M15/33—Esters containing fluorine
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06N—WALL, FLOOR, OR LIKE COVERING MATERIALS, e.g. LINOLEUM, OILCLOTH, ARTIFICIAL LEATHER, ROOFING FELT, CONSISTING OF A FIBROUS WEB COATED WITH A LAYER OF MACROMOLECULAR MATERIAL; FLEXIBLE SHEET MATERIAL NOT OTHERWISE PROVIDED FOR
- D06N3/00—Artificial leather, oilcloth or other material obtained by covering fibrous webs with macromolecular material, e.g. resins, rubber or derivatives thereof
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
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- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
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- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/08—Separating or sorting of material, associated with crushing or disintegrating
- B02C23/16—Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
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- Y02E50/10—Biofuels, e.g. bio-diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/249921—Web or sheet containing structurally defined element or component
- Y10T428/249924—Noninterengaged fiber-containing paper-free web or sheet which is not of specified porosity
Definitions
- This invention relates to fibrous materials and composites, and to methods of making the same.
- Fibrous materials e.g., cellulosic and lignocellulosic materials, are produced, processed, and used in large quantities in a number of applications. Often such fibrous materials are used once, and then discarded as waste.
- the invention relates to fibrous materials and composites, and to methods of making the same.
- a first aspect of the invention features fibrous materials and methods of making fibrous materials.
- Methods of making fibrous materials include shearing a fiber source to provide a first fibrous material, and passing the first fibrous material through a first screen having an average opening size of 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material.
- the average opening size of the first screen is less than about 0.79 mm ( 1/32 inch, 0.03125 inch), e.g., less than about 0.40 mm ( 1/64 inch, 0.015625 inch), less than about 0.20 mm ( 1/128 inch, 0.0078125 inch), or even less than about 0.10 mm ( 1/256 inch, 0.00390625 inch).
- the shearing is performed with a rotary knife cutter.
- the second fibrous material can, e.g., be collected in a bin having a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure or at least 75 percent below nominal atmospheric pressure.
- the second fibrous material can, e.g., be sheared once or numerous times, e.g., twice, thrice, or even more, e.g., ten times.
- the second fibrous material can, e.g., be sheared and the resulting fibrous material passed through the first screen.
- the second fibrous material can be sheared, and the resulting fibrous material passed through a second screen having an average opening size less than the first screen, providing a third fibrous material.
- a ratio of an average length-to-diameter ratio of the second fibrous material to an average length-to-diameter ratio of the third fibrous material can be, e.g., less than about 1.5, less than about 1.4, less than about 1.25, or even less than about 1.1.
- the second fibrous can, e.g., be passed through a second screen having an average opening size less than the first screen.
- the shearing and passing can, e.g., be performed concurrently.
- the second fibrous material can have an average length-to-diameter ratio of, e.g., greater than about 10/1, greater than about 25/1, or even greater than about 50/1.
- An average length of the second fibrous material can be, e.g., between about 0.5 mm and about 2.5 mm, e.g., between about 0.75 mm and about 1.0 mm.
- An average width of the second fibrous material can be, e.g., between about 5 ⁇ m and about 50 ⁇ m, e.g., between about 10 ⁇ m and about 30 ⁇ m.
- a standard deviation of a length of the second fibrous material can be less than about 60 percent of an average length of the second fibrous material, e.g., less than about 50 percent of an average length of the second fibrous material.
- a BET surface area of the second fibrous material is greater than about 0.5 m 2 /g, e.g., greater than about 1.0 m 2 /g, greater than about 1.5 m 2 /g, greater than about 1.75 m 2 /g, or even greater than about 0.5 m 2 /g.
- a porosity of the second fibrous material is greater than about 70 percent, e.g., greater than about 85 percent, or greater than about 90 percent.
- a ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter ratio of the second fibrous material is less than about 1.5, e.g., less than about 1.4, less than about 1.25, or less than about 1.1.
- the screen is formed by interweaving mono-filaments.
- the fiber source can include, e.g., a cellulosic material, a lignocellulosic material.
- the fiber source can be sawdust.
- the fiber source includes a blend of fibers, e.g., fibers derived from a paper source and fibers derived from a textile source, e.g., cotton.
- Methods of making fibrous materials include shearing a fiber source to provide a first fibrous material; and passing the fibrous material through a first screen to provide a second fibrous material.
- a ratio of an average length-to-diameter ratio of the first fibrous material to an average length-to-diameter of the second fibrous material is less than about 1.5.
- Methods of making fibrous materials include shearing a fiber source to provide a first fibrous material; passing the fibrous material through a first screen to provide a second fibrous material; and then shearing the second fibrous material again to provide a third fibrous material.
- Fibrous materials are disclosed that have an average length-to-diameter ratio of greater than about 5, and having a standard deviation of a fiber length of less than about sixty percent of an average fiber length.
- the average length-to-diameter ratio can be greater than about 10/1, e.g., greater than about 15/1, greater than about 25/1, greater than about 35/1, greater than about 45/1, or even greater than about 50/1.
- the average length can be between about 0.5 mm and about 2.5 mm.
- Methods of making fibrous materials include shearing a fiber source to provide a first fibrous material; collecting the first fibrous material; and then shearing the first fibrous to provide a second fibrous material.
- Composites are disclosed that includes a fibrous material, a resin and a dye.
- the dye can aid in the masking of the fibrous material in the composite.
- the fibrous material can have an average length-to-diameter ratio of greater than about 5, and a standard deviation of a fiber length of less than about sixty percent of an average fiber length.
- the composite additionally includes a pigment.
- the dye is soaked into or surfaced on the fibers.
- the composites can include a scent or a fragrance.
- Methods of making composites include dyeing a fibrous material; combining the fibrous material with a resin; and forming a composite from the combination.
- Methods of making composites include adding a dye to a resin to provide a dye/resin combination; combining the dye/resin combination with a fibrous material; and forming a composite from the dye/resin combination and fibrous material.
- Any composite can be, e.g., in the form of a stepping stool, pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes and crutches.
- the first aspect and/or embodiments of the first aspect can have any one of, or combinations of, the following advantages.
- the fibrous materials are easy to disperse, e.g., in a molten thermoplastic resin.
- the fibrous materials can have, e.g., a relatively narrow length and/or length-to-diameter ratio distribution, such that their properties are consistently defined.
- the fibers of the fibrous materials when blended with a molten resin, can modify the rheology of the molten resin in a consistent and predicable manner, resulting in resin/fibrous material combinations that are, e.g., easier to mold and extrude.
- the fibrous materials can easily pass through small openings or channels, such as those found in or associated with injection molds, e.g., gates or hot runners. Parts molded from such fibrous materials can exhibit a good surface finish, e.g., with few visible speckles of large particles and/or agglomerated particles, when that is desired.
- a second aspect of the invention features densified fibrous materials, methods of making the densified fibrous materials, and composites made from the densified fibrous materials.
- Methods of densifying fibrous materials include adding, to a fibrous material, a water soluble binder, a water swellable binder, and/or a binder having a glass transition temperature of less than about 25° C., to provide a fibrous material-binder combination.
- the fibrous material-binder combination is densified to provide a densified fibrous material having a bulk density that is at least about two times greater than the bulk density of the fibrous material, e.g., three times, four times, five times, six times, eight times, ten times, twelve times, twenty times or more, e.g., forty times greater.
- the bulk density of the densified material is at least about three times or about four times greater than the bulk density of the fibrous material.
- Methods of densifying fibrous materials include densifying a fibrous material derived at least in part from polycoated paper to provide a densified fibrous material having a bulk density that is at least about two times greater than the bulk density of the fibrous material, e.g., three times, four times, five times, six times, eight times, ten times, twelve times, twenty times or more, e.g., forty times greater.
- Densifying includes heating the fibrous material to a temperature of at least about 50° C.
- Methods of densifying fibrous materials include moving a fibrous material past a binder application area at which a binder is applied to provide a fibrous material-binder combination.
- the fibrous material-binder combination is densified to provide a densified fibrous material having a bulk density of at least about two times the bulk density of the fibrous material, e.g., three times, four times, five times, six times, eight times, ten times, twelve times, twenty times or more, e.g., forty times greater.
- Methods of densifying fibrous materials include evacuating air from a fibrous material to increase the bulk density of the fibrous material at least about two times.
- the method can include sealing the fibrous material in a container and evacuating air from the container.
- Pellets or chips are disclosed that include a densified fibrous material.
- the pellets or chips have a bulk density of at least 0.3 g/cm 3 .
- the densified fibrous material includes a cellulosic or lignocellulosic material and a water soluble binder, a water swellable binder, and/or binders having a glass transition temperature of less than about 25° C.
- the pellets or chips have, e.g., an average thickness between about 2 mm and about 20 mm, an average width of between about 2 mm and about 40 mm and an average length of between about 5 mm and about 40 mm.
- the pellets define a hollow inner portion, or a multi-lobal structure.
- Plate-like densified fibrous materials which have a bulk density of at least 0.3 g/cm 3 .
- the densified fibrous materials includes a cellulosic or lignocellulosic material.
- the plate like densified fibrous materials have, e.g., an average thickness between about 2 mm and about 20 mm, an average width of between about 2 mm and about 40 mm and an average length of between about 5 mm and about 40 mm.
- Methods of densifying fibrous materials include adding, to a fibrous material, a water soluble binder, a water swellable binder and/or a binders having a glass transition temperature of less than about 25° C., to provide a fibrous material-binder combination.
- the fibrous-binder combination includes less than about 25 weight percent binder, e.g., 15 weight percent, 10 weight percent, 5 weight percent or less than about 1 weight percent.
- the fibrous material-binder combination is densified to provide a densified fibrous material having a bulk density that is at least about two times greater than the bulk density of the fibrous material, e.g., three times, four times, five times, six times, eight times, ten times, twelve times, twenty times or more, e.g., about forty times greater.
- Methods of compressing fibrous materials feature positioning a fibrous material including a binder with respect to a member, e.g., between a first member and a second member, to provide an uncompressed composite, and compressing the uncompressed composite to provide a compressed composite.
- the compressing is performed using a single member and a support.
- Any densified fibrous material can be used to form any article disclosed herein.
- the densified fibrous materials can include a scent or a fragrance.
- the densified fibrous materials can, e.g., be used to make composites, or they can be used as themselves or along with additives, e.g., as controlled release matrices.
- Methods of densifying fibrous materials e.g., a cellulosic or lignocellulosic material, are also disclosed that do not utilize a binder.
- Pellets or chips of densified fibrous materials are disclosed that have a bulk density of at least about 0.3 g/cm 3 .
- the densified fibrous materials include a fibrous material other than a cellulosic or cellulosic material and a binder.
- the pellets or chips have an average thickness between about 2 mm and about 20 mm, an average width of between about 2 mm and about 40 mm and an average length of between about 5 mm and about 40 mm.
- Plate-like densified fibrous materials are disclosed that have a bulk density of at least about 0.3 g/cm 3 .
- the densified fibrous materials include a fibrous material other than a cellulosic or lignocellulosic material and a binder.
- the plate-like densified fibrous materials have an average thickness between about 2 mm and about 20 mm, an average width of between about 2 mm and about 40 mm and an average length of between about 5 mm and about 40 mm.
- the second aspect and/or embodiments of the second aspect can have any one of, or combinations of, the following advantages.
- the densified fibrous materials e.g., in pellet or chip form, are easier to handle, feed into machinery, transport, and mix with other materials, e.g., resins, e.g., thermoplastic resin.
- a third aspect of the invention features crosslinked composites, and composites that include nanometer scale fillers.
- the composites that include the nanometer scale fillers are optionally crosslinked when this is desired.
- Methods of making composites include combining a fibrous material with a radiation cross-linkable resin, e.g., a thermoplastic resin, to provide a fibrous material/cross-linkable resin combination.
- a radiation cross-linkable resin e.g., a thermoplastic resin
- the fibrous material has an average length-to-diameter ratio of greater than about 5, and a standard deviation of a fiber length is less than about eighty five percent of an average fiber length.
- the fibrous material/cross-linkable resin is irradiated, e.g., with an ionizing radiation, to at least partially cross-link the cross-linkable resin.
- the fibrous material/crosslinkable resin combination is formed into a desired shape.
- the radiation cross-linkable resin can be, e.g., a thermoplastic or a thermoset, e.g., a cast thermoset.
- the radiation cross-linkable resin can be a polyolefin, e.g., a polyethylene (e.g., a copolymer of polyethylene), a polypropylene (e.g., a copolymer of polypropylene), a polyester (e.g., polyethylene terephthalate), a polyamide (e.g., nylon 6, 6/12 or 6/10), a polyethyleneimine, elastomeric styrenic copolymers (e.g., styrene-ethylene-butylene-styrene copolymers), a polyamide elastomer (e.g., polyether-polyamide copolymer), ethylene-vinyl acetate copolymer, or compatible mixtures of these resins.
- a polyolefin e.
- the resin is a polyolefin that has a polydispersity of greater than about 2, e.g., greater than about 3, greater than about 3.5, greater than about 4.0, greater than about 4.5, greater than about 5.0, greater than about 7.5 or even greater than about 10.
- a high polydispersity can improve impact resistance in the cross-linked composite.
- the polyolefin has a melt flow rate greater than about 10, e.g., greater than 15, greater than 20, greater than 25, greater than 30, or even greater than about 50.
- a high melt flow can aid in the production of the composite, e.g., by reducing shear heating during the forming of the composite.
- the fibrous material is provided by shearing a fiber source, e.g., sawdust from milling a hard or soft wood (e.g., oak, cedar or redwood).
- a fiber source e.g., sawdust from milling a hard or soft wood (e.g., oak, cedar or redwood).
- the average length-to-diameter ratio of the fibers of the fibrous materials can be, e.g., greater than about 10/1, e.g., greater than 15/1, greater than 25/1, or even greater than about 50/1.
- a high L/D can improve the mechanical properties, e.g., tensile strength and flexural modulus of the composite.
- the standard deviation of the fiber length is less than about seventy-five percent of the average fiber length, e.g., less than fifty percent, less than 35 percent, less than 25 percent, less than 15 percent, less than 10 percent, less than 5 percent, or even less than about 2.5 percent.
- a low standard deviation can, e.g., improve processability of the fibrous material/resin blend.
- An average length of the fibrous material can be, e.g., between about 0.5 mm and about 2.5 mm, e.g., between about 0.75 mm and about 1.0 mm.
- An average width of the fibrous material is between about 5 ⁇ m and about 50 ⁇ m, e.g., between about 10 ⁇ m and about 30 ⁇ m.
- the fibrous material can be, e.g., derived from a textile, e.g., cotton scraps or remnants, a paper source, a plant or a tree.
- the fibrous material includes a blend of fibers, e.g., fibers derived from a paper source and fibers derived from a textile source, e.g., cotton.
- the irradiating of the fibrous material/cross-linkable resin combination is performed with gamma rays or a beam of electrons.
- the composite is in the form of a structure, ornamental goods and articles, a stepping stool, pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes and crutches.
- the fibrous material is prepared by shearing a fiber source to provide a first fibrous material, and passing the first fibrous material through a first screen having an average opening size of about 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second material.
- the average opening size of the first screen is less than 0.79 mm ( 1/32 inch, 0.03125 inch), e.g., less than about 0.40 mm ( 1/64 inch, 0.015625 inch).
- the irradiating is performed with electromagnetic radiation that has an energy per photon (in electron volts) of greater than about 10 2 eV/photon, e.g., greater than 10 3 , 10 4 , 10 5 , 10 6 , or even greater than about 10 7 eV/photon.
- the electromagnetic radiation has energy per photon of between about 10 4 and about 10 7 , e.g., between about 10 5 and about 10 6 eV/photon.
- the irradiating is performed with electromagnetic radiation that has a frequency of greater than about 10 16 hz, greater than about 10 17 hz, 10 18 , 10 19 , 10 20 , or even greater than about 10 21 hz.
- the electromagnetic radiation has a frequency of between about 10 18 and about 10 22 , e.g., between about 10 19 to about 10 21 hz.
- the irradiating is performed until the fibrous material/cross-linkable resin combination receives a dose of at least about 0.25 Mrad, e.g., at least 1.0 Mrad, at least 2.5 Mrad, at least 5.0 Mrad, or at least about 10 Mrad. In some embodiments, the irradiating is performed until the fibrous material/cross-linkable resin combination receives a dose of between about 1.0 Mrad and about 6.0 Mrad, e.g., between about 1.5 Mrad and about 4.0 Mrad.
- the irradiating is performed at a dose rate of between 5 about 5 and about 1500 kilorads/hour, e.g., between about 10 and about 750 kilorads/hour or between about 50 and about 350 kilorads/hours.
- the irradiating is performed with electromagnetic radiation generated from a 60 Co source.
- Composites include a cross-linked resin and a fibrous material having an average length-to-diameter ratio of greater than about 5 and a standard deviation of a fiber length is less than about eighty five percent of an average fiber length.
- the average length-to-diameter ratio is greater than about 10/1, e.g., greater than about 15/1, greater than about 25/1, or even greater than 5 about 0/1.
- the standard deviation the fiber length is less than about seventy-five percent of the average fiber length, e.g., less than fifty percent, less than 35 percent, less than 25 percent, less than 15 percent, less than 10 percent, less than 5 percent, or even less than about 2.5 percent.
- an average length of the fibrous material is between about 5 mm and about 2.5 mm, e.g., between about 5 ⁇ m and about 50 ⁇ m.
- Methods of making composites also are disclosed that include shearing a fiber source to provide a fibrous material; combining the fibrous material with a cross-linkable resin to provide a fibrous material/resin combination; and irradiating with gamma radiation to at least partially crosslink the cross-linkable resin.
- the shearing is performed with a rotary knife cutter.
- Methods of making composites include combining a fibrous material with a radiation cross-linkable resin to provide a fibrous material/cross-linkable resin combination.
- the fibrous material has an average length-to-diameter ratio of greater than about 5, and a standard deviation of a fiber length is less than about eighty five percent of an average fiber length.
- the fibrous material/cross-linkable resin is formed into a desired shape and irradiated to at least partially cross-link the cross-linkable resin.
- Methods of making composites include combining a filler, e.g., a fibrous material, with a radiation cross-linkable resin to provide a filler/cross-linkable resin combination and irradiating the filler/cross-linkable resin combination to at least partially cross-link the cross-linkable resin.
- a filler e.g., a fibrous material
- Methods of reducing biological overgrowth, e.g., of yeasts and/or bacteria, in composites include irradiating a composite with an ionizing radiation prior to use.
- the composite is in the form of a board, e.g., decking material.
- Composites include a resin, a filler having a transverse dimension of less than about 1000 nm, and a fibrous material.
- the transverse dimension is less than 500 nm.
- the resin is cross-linked, e.g., using a chemical cross-linking agent or radiation.
- the fibrous material includes a cellulosic or lignocellulosic material.
- the fibrous material has an average length-to-diameter ratio of greater than about 5 and a standard deviation of a fiber length is less than about eighty five percent of an average fiber length.
- Methods of making composites include combining a filler having a transverse dimension of less than about 1000 nm and a fibrous material with a resin.
- the methods may further include forming the combination of the filler/fibrous material/resin into a desired shape.
- the desired shape can be, e.g., irradiated to at least partially cross-link the resin.
- Methods of making composites include combining a filler having a transverse dimension of less than about 1000 nm and a fibrous material with a radiation cross-linkable resin to provide a filler/fibrous material/cross-linkable resin combination; and irradiating the filler/fibrous material/cross-linkable resin combination to at least partially cross-link the cross-linkable resin.
- Composites are also disclosed that include a resin and sawdust having fibers having an average length-to-diameter ratio of greater than about 5 and a standard deviation of a fiber length is less than about eighty five percent of an average fiber length dispersed therein.
- the sawdust is derived from a hard wood, e.g., oak, or from a soft wood, e.g., cedar, redwood or pine.
- Methods of making composites include shearing sawdust to provide a fibrous material, and combining the fibrous material with a resin to provide a fibrous material/resin combination.
- the methods may further include irradiating the fibrous material/resin combination with gamma radiation to at least partially crosslink the resin.
- the third aspect and/or embodiments of the third aspect can have any one of, or combinations of, the following advantages.
- the composites can have excellent mechanical properties, e.g., abrasion resistance, compression strength, fracture resistance, impact strength, bending strength, tensile modulus, flexural modulus and elongation at break.
- the composites can have excellent low temperature performance, e.g., having a reduced tendency to break and/or crack at low temperatures, e.g., temperatures below 0° C., e.g., below ⁇ 110° C., ⁇ 20° C., ⁇ 40° C., ⁇ 50° C., ⁇ 60° C. or even below ⁇ 100° C.
- the composites can have excellent performance at high temperatures, e.g., maintain their advantageous mechanical properties at relatively high temperature, e.g., at temperatures above 100° C., e.g., above 125° C., 150° C., 200° C., 250° C., 300° C., 400° C., or even above 500° C.
- the composites can have excellent chemical resistance, e.g., resistance to swelling in a solvent, e.g., a hydrocarbon solvent, resistance to chemical attack, e.g., by strong acids, strong bases, strong oxidants (e.g., chlorine or bleach) or reducing agents (e.g., active metals such as sodium and potassium).
- the composites can have a reduced tendency rot and decay since treatment of the composites with radiation tends to kill any microbes, e.g., fungus, bacteria or insects.
- a fourth aspect of the invention features fragranced composites, and methods of making the same.
- the fragranced composites can be crosslinked if this is desired.
- Fiber sources, fibrous materials or densified fibrous materials are disclosed in combination with a fragrance.
- fragrances include cedarwood, evergreen or redwood.
- the fiber source, the fibrous material or the densified fibrous material in combination with the fragrance includes a colorant and/or a biocide.
- the fragrance includes a tree fragrance, e.g., natural redwood fragrance, and the color, e.g., red, matches the tree from which the fragrance is derived.
- Fiber sources, fibrous materials or densified fibrous materials are also disclosed in combination with a fragrance and a resin, e.g., a thermoplastic resin.
- a colorant and/or a biocide is also utilized.
- the fragrance includes a tree fragrance, e.g., natural redwood fragrance, and the color, e.g., red, matches the tree from which the fragrance is derived.
- Methods of making composites include adding to a fibrous material to a fragrance to provide a fibrous material-fragrance combination, and compressing the fibrous material-fragrance combination to provide a composite.
- the fragrance can be, e.g., in a resin that is added to the fibrous material.
- Composites are also disclosed that include a fibrous material and a fragrance.
- the composites also includes a resin, e.g., a thermoplastic or thermoset resin.
- the fibers of the fibrous material can have, e.g., a length-to-diameter ratio of greater than about 5, e.g., greater than 10, greater than 25, greater than 50 or greater than about 100.
- the fourth aspect and/or embodiments of the fourth aspect can have any one of, or combinations of, the following advantages.
- the disclosed scented composites e.g., densified fibrous materials and wood-substitute composites, can stir interest at a point of purchase, and can allow for unusual branding and marketing opportunities.
- a fifth aspect of the invention features composites that have unique, pleasing or even striking visual properties, and methods of making the same.
- Composite include a resin and a fibrous material, and that have an external surface. Some of the fibrous material is visible.
- the fibrous material can be visible on the external surface, in the external surface, or under the external surface, e.g., under the surface a distance of less than about 0.100 inch, e.g., less than 0.050 inch, less than 0.025 inch, less than 0.010 inch or less than about 0.005 inch.
- Composites include a transparent resin, e.g., transparent nylon or clarified polypropylene, and a fibrous material.
- Method of making composites include combining a resin and a fibrous material to provide a resin/fibrous material combination; and compressing the resin/fibrous material combination to provide a composite having an external surface in which some of the fibrous material is visible.
- Methods of making composites include combining a transparent resin and a fibrous material to provide a transparent resin/fibrous material combination; and compressing the transparent resin/fibrous material combination to provide a composite.
- the fifth aspect and/or embodiments of the fifth aspect can have any one of, or combinations of, the following advantages.
- the composites can have unique, pleasing or even striking visual properties, and at the same time can have desirable mechanical properties, e.g., high abrasion resistance, high compression strength, fracture resistance, high impact strength, high bending strength, high tensile modulus, high flexural modulus and high elongation at break.
- Such composites can, e.g., enhance brand name recognition and brand name loyalty.
- fibrous material is a material that includes numerous loose, discrete and separable fibers.
- a fibrous material can be prepared from a polycoated paper or a bleached Kraft paper fiber source by shearing, e.g., with a rotary knife cutter.
- screen means a member capable of sieving material according to size, e.g., a perforated plate, cylinder or the like, or a wire mesh or cloth fabric.
- a nanometer scale filler is one that has a transverse dimension of less than about 1000 nm.
- the transverse dimension of a nanometer scale filler is its diameter if it is a spherical particle or a relatively long thin fiber, or a maximum size of an irregularly shaped particle.
- a fibrous material is visible on or in a composite if the fibrous material can be seen by a human being of average vision under daylight conditions when the composite is held a distance of three feet from the human.
- FIG. 1 is block diagram illustrating conversion of a fiber source into a first and second fibrous material.
- FIG. 2 is a cross-sectional view of a rotary knife cutter.
- FIGS. 3-8 are top views of a variety of screens made from monofilaments.
- FIG. 9 is block diagram illustrating conversion of a fiber source into a first, second and third fibrous material.
- FIGS. 10A and 10B are photographs of fiber sources; FIG. 10A being a photograph of a polycoated paper container, and FIG. 10B being a photograph of unbleached Kraft paper rolls.
- FIGS. 11 and 12 are scanning electron micrographs of a fibrous material produced from polycoated paper at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- the fibrous material was produced on a rotary knife cutter utilizing a screen with 1 ⁇ 8 inch openings.
- FIGS. 13 and 14 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- the fibrous material was produced on a rotary knife cutter utilizing a screen with 1 ⁇ 8 inch openings.
- FIGS. 15 and 16 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- the fibrous material was twice sheared on a rotary knife cutter utilizing a screen with 1/16 inch openings during each shearing.
- FIGS. 17 and 18 are scanning electron micrographs of a fibrous material produced from bleached Kraft board paper at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- the fibrous material was thrice sheared on a rotary knife cutter. During the first shearing, a 1 ⁇ 8 inch screen was used; during the second shearing, a 1/16 inch screen was used, and during the third shearing a 1/32 inch screen was used.
- FIG. 19 is block diagram illustrating conversion of a fiber source into a fibrous material, and then densification of the fibrous material.
- FIG. 20 is a densified fibrous material in pellet form.
- FIG. 20A is a transverse cross-section of a hollow pellet in which a center of the hollow is in-line with a center of the pellet.
- FIG. 20B is a transverse cross-section of a hollow pellet in which a center of the hollow is out of line with the center of the pellet.
- FIG. 20C is a transverse cross-section of a tri-lobal pellet.
- FIG. 21 is a block diagram illustrating revertible bulk densification.
- FIG. 22 is schematic side view of a process for coating a fibrous material with a binder and/or adding additives to the fibrous material.
- FIG. 23 is a schematic side view of a process for forming a densified fibrous material.
- FIG. 24 is a perspective view in cut-away of a pellet mill.
- FIG. 25 is a schematic side view of a process for manufacturing a densified fibrous material.
- FIG. 25A is an enlarged view of area 25 A of FIG. 25 .
- FIG. 26 is a block diagram illustrating conversion of a fibrous material/cross-linkable resin combination into a desired shape, and irradiating the desired shape to form a cross-linked composite.
- FIG. 27 is a perspective, cut-away view of a gamma irradiator.
- FIG. 28 is an enlarged perspective view of region 28 of FIG. 27 .
- FIG. 29 is a photograph of a resin/fibrous material composite in the form of a step stool in which some of the fibrous material of the composite is visible.
- FIG. 30 is an enlarged view of the box region of FIG. 29 .
- FIGS. 31A , 31 B and 31 C schematically illustrate making a composite from a mold having a mold surface.
- FIG. 32 is a cross-sectional view of resin/fibrous material composite having an inner portion that has substantially no fibrous material and an outer portion surrounding the inner portion that includes fibrous material.
- FIG. 33 is a cross-sectional view of a transparent resin/fibrous material composite having an inner portion that has substantially all of the fibrous material and an outer portion having substantially no fibrous material surrounding the inner portion.
- fibrous materials Generally, fibrous materials, densified fibrous materials and composites made from these materials and combinations of these materials are disclosed.
- Some of the fibrous materials disclosed herein are easy to disperse in a resin, such as a thermoplastic resin, and can advantageously modify the rheology of the resin in a consistent and predicable manner, resulting in resin/fibrous material combinations that can be, e.g., easier to mold and extrude.
- a resin such as a thermoplastic resin
- Many of the densified fibrous materials disclosed herein, such as those in pellet or chip form, can be easier to handle, feed into machinery, transport, and mix with other materials.
- Many of the composites disclosed herein have excellent mechanical properties, such as abrasion resistance, compression strength, fracture resistance, impact strength, bending strength, tensile modulus, flexural modulus and elongation at break.
- the composites and especially many of the crosslinked composites, have a reduced tendency to break and/or crack at low temperatures and have enhanced high temperature stability and chemical resistance.
- Some of the scented composites such as wood-substitute composites, can stir interest at a point of purchase, and can allow for unusual branding and marketing opportunities.
- Many disclosed composites have unique, pleasing or even striking visual properties.
- fibrous materials are derived from one or more fiber sources, e.g., by shearing a fiber source to release fibrous material.
- a fiber source 10 is sheared, e.g., in a rotary knife cutter, to provide a first fibrous material 12 .
- This fibrous material can be used as provided, e.g., to make densified fibrous materials and/or composites, or the first fibrous material 12 can be passed through a first screen 16 having an average opening size of 1.59 mm or less ( 1/16 inch, 0.0625 inch) to provide a second fibrous material 14 .
- fiber source 10 can be cut prior to the shearing, e.g., with a shredder.
- the paper when a paper is used as the fiber source 10 , the paper can be first cut into strips that are, e.g., 1 ⁇ 4- to 1 ⁇ 2-inch wide, using a shredder, e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N.Y.).
- a shredder e.g., a counter-rotating screw shredder, such as those manufactured by Munson (Utica, N.Y.).
- the shearing of fiber source 10 and the passing of the resulting first fibrous material 12 through first screen 16 are performed concurrently.
- the shearing and the passing can also be performed in a batch-type process.
- a rotary knife cutter can be used to concurrently shear the fiber source 10 and screen the first fibrous material 12 .
- a rotary knife cutter 20 includes a hopper 22 that can be loaded with a shredded fiber source 10 ′ prepared by shredding fiber source 10 .
- Shredded fiber source 10 ′ is sheared between stationary blades 24 and rotating blades 26 to provide a first fibrous material 12 .
- First fibrous material 12 passes through screen 16 having the dimensions described above, and the resulting second fibrous material 14 is captured in bin 30 .
- bin 30 can have a pressure below nominal atmospheric pressure, e.g., at least 10 percent below nominal atmospheric pressure, e.g., at least 25 percent below nominal atmospheric pressure, at least 50 percent below nominal atmospheric pressure, or at least 75 percent below nominal atmospheric pressure.
- a vacuum source 50 is utilized to maintain the bin below nominal atmospheric pressure.
- the average opening size of the first screen 16 is less than 0.79 mm ( 1/32 inch, 0.03125 inch), e.g., less than 0.51 mm ( 1/50 inch, 0.02000 inch), less than 0.40 mm ( 1/64 inch, 0.015625 inch), less than 0.23 mm (0.009 inch), less than 0.20 mm ( 1/128 inch, 0.0078125 inch), less than 0.18 mm (0.007 inch), less than 0.13 mm (0.005 inch), or even less than less than 0.10 mm ( 1/256 inch, 0.00390625 inch).
- Screen 16 is prepared by interweaving monofilaments 52 having an appropriate diameter to give the desired opening size.
- the monofilaments can be made of a metal, e.g., stainless steel.
- a metal e.g., stainless steel.
- the screens can be made from monofilaments made from a material other than stainless steel, e.g., titanium, titanium alloys, amorphous metals, nickel, tungsten, rhodium, rhenium, ceramics, or glass.
- the screen is made from a plate, e.g. a metal plate, having apertures, e.g., cut into the plate using a laser.
- the second fibrous 14 is sheared and passed through the first screen 16 , or a different sized screen. In some embodiments, the second fibrous material 14 is passed through a second screen having an average opening size equal to or less than that of first screen 16 .
- a third fibrous material 62 can be prepared from the second fibrous material 14 by shearing the second fibrous material 14 and passing the resulting material through a second screen 60 having an average opening size less than the first screen 16 .
- Suitable fiber sources include cellulosic fiber sources, including paper and paper products like those shown in FIGS. 10A (polycoated paper) and 10 B (Kraft paper), and lignocellulosic fiber sources, including wood, and wood-related materials, e.g., particle board.
- Fiber sources include natural fiber sources, e.g., grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice hulls, coconut hair; fiber sources high in ⁇ -cellulose content, e.g., cotton; synthetic fiber sources, e.g., extruded yarn (oriented yarn or un-oriented yarn) or carbon fiber sources; inorganic fiber sources; and metal fiber sources. Natural or synthetic fiber sources can be obtained from virgin scrap textile materials, e.g., remnants or they can be post consumer waste, e.g., rags.
- natural fiber sources e.g., grasses, rice hulls, bagasse, cotton, jute, hemp, flax, bamboo, sisal, abaca, straw, corn cobs, rice hulls, coconut hair
- fiber sources high in ⁇ -cellulose content e.g., cotton
- synthetic fiber sources e.g., extruded yarn (
- paper products When paper products are used as fiber sources, they can be virgin materials, e.g., scrap virgin materials, or they can be post-consumer waste. Additional fiber sources have been described in U.S. Pat. Nos. 6,448,307, 6,258,876, 6,207,729, 5,973,035 and 5,952,105.
- the fiber source includes sawdust, e.g., from milling, machining or sanding hard or soft woods.
- hard woods include oak, maple, cherry (e.g., Brazilian cherry), walnut, mahogany, cypress or rosewood.
- soft woods include cedar (e.g., red and white cedar), pine, spruce, fir (e.g., Douglas fir) and redwood.
- cedar e.g., red and white cedar
- pine spruce
- fir e.g., Douglas fir
- redwood e.g., pine
- spruce e.g., Douglas fir
- fragrance is added to the sawdust.
- shear the sawdust e.g., using a rotary knife cutter, to de-agglomerate the sawdust.
- Blends of any of the above fiber sources or fibrous materials can be utilized, e.g., to make composites or densified fibrous materials.
- the fibers of the fibrous materials can have a relatively large average length-to-diameter ratio (e.g., greater than 20-to-1), even if they have been sheared more than once.
- the fibers of the fibrous materials described herein may have a relatively narrow length and/or length-to-diameter ratio distribution.
- the relatively large average length-to-diameter ratio and the relatively narrow length and/or length-to-diameter ratio distribution are, at least in part, responsible for the ease at which the fibrous materials are dispersed in a resin, e.g., a molten thermoplastic resin.
- average fiber widths are those determined optically by randomly selecting approximately 5,000 fibers.
- Average fiber lengths are corrected length-weighted lengths.
- BET Brunauer, Emmet and Teller
- surface areas are multi-point surface areas, and porosities are those determined by mercury porosimetry.
- the average length-to-diameter ratio of the second fibrous material 14 can be, e.g. greater than 10/1, e.g., greater than 25/1 or greater than 50/1.
- An average length of the second fibrous material 14 can be, e.g., between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm, and an average width (i.e., diameter) of the second fibrous material 14 can be, e.g., between about 5 ⁇ m and 50 ⁇ m, e.g., between about 10 ⁇ m and 30 ⁇ m.
- a standard deviation of the length of the second fibrous material 14 is less than 60 percent of an average length of the second fibrous material 14 , e.g., less than 50 percent of the average length, less than 40 percent of the average length, less than 25 percent of the average length, less than 10 percent of the average length, less than 5 percent of the average length, or even less than 1 percent of the average length.
- a BET surface area of the second fibrous material 14 is greater than 0.5 m 2 /g, e.g., greater than 1.0 m 2 /g, greater than 1.5 m 2 /g, greater than 1.75 m 2 /g or even greater than 5.0 m 2 /g.
- a porosity of the second fibrous material 14 can be, e.g., greater than 70 percent, e.g., greater than 80 percent, greater than 85 percent or greater than 90 percent.
- a ratio of the average length-to-diameter ratio of the first fibrous material 12 to the average length-to-diameter ratio of the second fibrous material 14 is, e.g., less than 1.5, e.g., less than 1.4, less than 1.25, or even less than 1.1.
- the second fibrous material 14 is sheared again and the resulting fibrous material passed through a second screen having an average opening size less than the first screen to provide a third fibrous material 62 .
- a ratio of the average length-to-diameter ratio of the second fibrous material 14 to the average length-to-diameter ratio of the third fibrous material 62 can be, e.g., less than 1.5, e.g., less than 1.4, less than 1.25, or even less than 1.1.
- the third fibrous material 62 is passed through a third screen to produce a fourth fibrous material.
- the fourth fibrous material can be, e.g., passed through a fourth screen to produce a fifth material. Similar screening processes can be repeated as many times as desired to produce the desired fibrous material having the desired properties.
- the desired fibrous material includes fibers having an average length-to-diameter ratio of greater than 5 and having a standard deviation of the fiber length that is less than sixty percent of the average length.
- the average length-to-diameter ratio can be greater than 10/1, e.g., greater than 25/1, or greater than 50/1, and the average length can be between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 nm.
- An average width of the fibrous material can be between about 5 ⁇ m and 50 ⁇ m, e.g., between about 10 ⁇ m and 30 ⁇ m.
- the standard deviation can be less than 50 percent of the average length, e.g., less than 40 percent, less than 30 percent, less than 25 percent, less than 20 percent, less than 10 percent, less than 5 percent, or even less than 1 percent of the average length.
- a desirable fibrous material can have, e.g., a BET surface area of greater than 0.5 m 2 /g, e.g., greater than 1.0 m 2 /g, greater than 1.5 m 2 /g, greater than 1.75 m 2 /g., greater than 5 m 2 /g, or even greater than 10 m 2 /g.
- a desired material can have, e.g., a porosity of greater than 70 percent, e.g., greater than 80 percent, greater than 87.5 percent, greater than 90 percent, or even greater than 95 percent.
- a fiber source can be sheared between a first pair of blades that defines a first gap, resulting in a first fibrous material.
- the first fibrous material can then be sheared between a second pair of blades that define a second gap that is smaller than the first gap, resulting in a second fibrous material.
- Fiber lengths and widths were determined by Integrated Paper Services, Inc., Appleton, Wis., using an automated analyzer (TAPPI T271).
- BET surface area were determined by Micromeritics Analytical Services, as were porosity and bulk density.
- a 1500 pound skid of virgin, half-gallon juice cartons made of un-printed polycoated white Kraft board having a bulk density of 20 lb/ft 3 was obtained from International Paper. Each carton was folded flat, and then fed into a 3 hp Flinch Baugh shredder at a rate of approximately 15 to 20 pounds per hour.
- the shredder was equipped with two 12 inch rotary blades, two fixed blades and a 0.30 inch discharge screen. The gap between the rotary and fixed blades was adjusted to 0.10 inch.
- the output from the shredder resembled confetti having a width of between 0.1 inch and 0.5 inch, a length of between 0.25 inch and 1 inch and a thickness equivalent to that of the starting material (about 0.075 inch).
- the confetti-like material was fed to a Munson rotary knife cutter, Model SC30.
- Model SC30 is equipped with four rotary blades, four fixed blades, and a discharge screen having 1 ⁇ 8 inch openings.
- the gap between the rotary and fixed blades was set to approximately 0.020 inch
- the rotary knife cutter sheared the confetti-like pieces across the knife-edges, tearing the pieces apart and releasing a fibrous material at a rate of about one pound per hour.
- the fibrous material had a BET surface area of 0.9748 m 2 /g+/ ⁇ 0.0167 m 2 /g, a porosity of 89.0437 percent and a bulk density (@0.53 psia) of 0.1260 g/mL.
- An average length of the fibers was 1.141 mm and an average width of the fibers was 0.027 mm, giving an average L/D of 42:1.
- Scanning electron micrographs of the fibrous material are shown in FIGS. 11 and 12 at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft 3 was obtained from International Paper.
- the material was folded flat, and then fed into a 3 hp Flinch Baugh shredder at a rate of approximately 15 to 20 pounds per hour.
- the shredder was equipped with two 12 inch rotary blades, two fixed blades and a 0.30 inch discharge screen. The gap between the rotary and fixed blades was adjusted to 0.10 inch.
- the output from the shredder resembled confetti having a width of between 0.1 inch and 0.5 inch, a length of between 0.25 inch and 1 inch and a thickness equivalent to that of the starting material (about 0.075 inch).
- the confetti-like material was fed to a Munson rotary knife cutter, Model SC30.
- the discharge screen had 1 ⁇ 8 inch openings.
- the gap between the rotary and fixed blades was set to approximately 0.020 inch.
- the rotary knife cutter sheared the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour.
- the fibrous material bad a BET surface area of 1.1316 m 2 /g+/ ⁇ 0.0103 m 2 /g, a porosity of 88.3285 percent and a bulk density (@0.53 psia) of 0.1497 g/mL.
- An average length of the fibers was 1.063 mm and an average width of the fibers was 0.0245 mm, giving an average L/D of 43:1.
- Scanning electron micrographs of the fibrous material are shown in FIGS. 13 and 14 at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft 3 was obtained from International Paper.
- the material was folded flat, and then fed into a 3 hp Flinch Baugh shredder at a rate of approximately 15 to 20 pounds per hour.
- the shredder was equipped with two 12 inch rotary blades, two fixed blades and a 0.30 inch discharge screen. The gap between the rotary and fixed blades was adjusted to 0.10 inch.
- the output from the shredder resembled confetti (as above).
- the confetti-like material was fed to a Munson rotary knife cutter, Model SC30.
- the discharge screen had 1/16 inch openings.
- the gap between the rotary and fixed blades was set to approximately 0.020 inch.
- the rotary knife cutter the confetti-like pieces, releasing a fibrous material at a rate of about one pound per hour.
- the material resulting from the first shearing was fed back into the same setup described above and sheared again.
- the resulting fibrous material bad a BET surface area of 1.4408 m 2 /g+/ ⁇ 0.0156 m 2 /g, a porosity of 90.8998 percent and a bulk density (@0.53 psia) of 0.1298 g/mL.
- An average length of the fibers was 0.891 mm and an average width of the fibers was 0.026 mm, giving an average L/D of 34:1. Scanning electron micrographs of the fibrous material are shown in FIGS. 15 and 16 at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- a 1500 pound skid of virgin bleached white Kraft board having a bulk density of 30 lb/ft 3 was obtained from International Paper.
- the material was folded flat, and then fed into a 3 hp Flinch Baugh shredder at a rate of approximately 15 to 20 pounds per hour.
- the shredder was equipped with two 12 inch rotary blades, two fixed blades and a 0.30 inch discharge screen. The gap between the rotary and fixed blades was adjusted to 0.10 inch.
- the output from the shredder resembled confetti (as above).
- the confetti-like material was fed to a Munson rotary knife cutter, Model SC30.
- the discharge screen had 1 ⁇ 8 inch openings.
- the gap between the rotary and fixed blades was set to approximately 0.020 inch.
- the rotary knife cutter sheared the confetti-like pieces across the knife-edges.
- the material resulting from the first shearing was fed back into the same setup and the screen was replaced with a 1/16 inch screen. This material was sheared.
- the material resulting from the second shearing was fed back into the same setup and the screen was replaced with a 1/32 inch screen. This material was sheared.
- the resulting fibrous material had a BET surface area of 1.6897 m 2 /g+/ ⁇ 0.0155 m 2 /g, a porosity of 87.7163 percent and a bulk density (@0.53 psia) of 0.1448 g/mL.
- An average length of the fibers was 0.824 mm and an average width of the fibers was 0.0262 mm, giving an average L/D of 32:1.
- Scanning electron micrographs of the fibrous material are shown in FIGS. 17 and 18 at 25 ⁇ magnification and 1000 ⁇ magnification, respectively.
- a fiber source is converted to a fibrous material.
- the fibrous material is subsequently densified.
- a binder and, optionally, other additives, such as fillers and anti-static materials, are added to the fibrous material prior to densification.
- the fibrous material with binder and any desired additives or fillers is densified by application of pressure, e.g., by passing the fibrous material through a nip defined between counter-rotating pressure rolls by passing the fibrous material through a pellet mill, or by compounding the fibrous material and binder in an extruder (e.g., a single screw or double screw extruder).
- heat can optionally be applied to aid in the densification of the fibrous material.
- the fiber source can be converted to the fibrous material, e.g., by mechanical means, e.g., cutting or shearing the fiber source, as discussed above.
- the fibers of the fibrous material can have, e.g., an average length-to-diameter ratio (L/D) of greater than 3, e.g., 5, 6, 7, 8, 10, 10, 25, 50, or more, e.g., 100.
- L/D average length-to-diameter ratio
- the fibers of the fibrous material have an average length of, e.g., 0.25 mm or more, e.g., 0.3 mm, 0.5 mm, 0.75 mm, 1 mm, 2 mm, 3 mm, 4 mm, 5 mm or more, e.g., 10 mm, and a maximum transverse dimension of greater than 0.05 mm, e.g., 0.075 mm, 0.1 mm, 0.2 mm, 0.3 mm, 0.4 mm, 0.5 mm or more, e.g., 1 mm.
- the fibers of the fibrous material may be separated, e.g., by screening, into fractions having different L/D ratios.
- the fibrous material prior to densification has a bulk density of less than 0.25 g/cm 3 , e.g., 0.20 g/cm 3 , 0.15 g/cm 3 , 0.10 g/cm 3 , 0.05 g/cm 3 or less, e.g., 0.025 g/cm 3 .
- Bulk density is determined using ASTM D1895B. Briefly, the method involves filling a measuring cylinder of known volume with a sample and obtaining a weight of the sample. The bulk density is calculated by dividing the weight of the sample in grams by the known volume of the cylinder in cubic centimeters.
- the fibrous material can be optionally treated, e.g., chemically treated or steam treated, to render the fibers of the fibrous material lipophilic, lipophobic, more adherent, and/or more dispersible or processable.
- the fibrous material can plasma treated or chemically treated with, e.g., silanes.
- the preferred binders include binders that are soluble in water, swollen by water, or that has a glass transition temperature of less 25° C., as determined by differential scanning calorimetry.
- water-soluble binders we mean binders having a solubility of at least about 0.05 weight percent in water.
- water swellable binders we mean binders that increase in volume by more than 0.5 percent upon exposure to water.
- the binders that are soluble or swollen by water include a functional group that is capable of forming a bond, e.g., a hydrogen bond, with the fibers of the fibrous material, e.g., cellulosic fibrous material.
- the functional group can be a carboxylic acid group, a carboxylate group, a carbonyl group, e.g., of an aldehyde or a ketone, a sulfonic acid group, a sulfonate group, a phosphoric acid group, a phosphate group, an amide group, an amine group, a hydroxyl group, e.g., of an alcohol, and combinations of these groups, e.g., a carboxylic acid group and a hydroxyl group.
- Specific monomeric examples include glycerin, glyoxal, ascorbic acid, urea, glycine, pentaerythritol, a monosaccharide or a disaccharide, citric acid, and tartaric acid.
- Suitable saccharides include glucose, sucrose, lactose, ribose, fructose, mannose, arabinose and erythrose.
- Polymeric examples include polyglycols, polyethylene oxide, polycarboxylic acids, polyamides, polyamines and polysulfonic acids polysulfonates.
- polymeric examples include polypropylene glycol (PPG), polyethylene glycol (PEG), polyethylene oxide, e.g., POLYOX®, copolymers of ethylene oxide and propylene oxide, polyacrylic acid (PAA), polyacrylamide, polypeptides, polyethylenimine, polyvinylpyridine, poly(sodium-4-styrenesulfonate) and poly(2-acrylamido-methyl-1-propanesulfonic acid).
- PPG polypropylene glycol
- PEG polyethylene glycol
- POLYOX® polyethylene oxide
- PAA polyacrylic acid
- PAA polyacrylamide
- polypeptides polyethylenimine
- polyvinylpyridine poly(sodium-4-styrenesulfonate)
- poly(2-acrylamido-methyl-1-propanesulfonic acid) poly(2-acrylamido-methyl-1-propanesulfonic acid).
- the binder includes a polymer that has a glass transition temperature less 25° C.
- polymers include thermoplastic elastomers (TPEs).
- TPEs include polyether block amides, such as those available under the tradename PEBAX®, polyester elastomers, such as those available under the tradename HYTREL®, and styrenic block copolymers, such as those available under the tradename KRATON®.
- the fibrous material includes ethylene vinyl acetate copolymer (EVA), polyolefins, e.g., polyethylene, polypropylene, ethylene-propylene copolymers, and copolymers of ethylene and alpha olefins, e.g., 1-octene, such as those available under the tradename ENGAGE®.
- EVA ethylene vinyl acetate copolymer
- polyolefins e.g., polyethylene, polypropylene, ethylene-propylene copolymers
- copolymers of ethylene and alpha olefins e.g., 1-octene
- the fibrous material is densified without the addition of a separate low glass transition temperature polymer.
- fibrous material made from polycoated paper can be densified by heating to above about 50° C., e.g., 75° C., 80° C., 90° C., 100° C.
- pressure during the heating e.g., pressure greater than about 50 lb/in 2 , e.g., 100 lb/in 2 , 250 lb/in 2 , 500 lb/in 2 , 1000 lb/in 2 or higher, e.g., 2500 lb/in 2 .
- the binder is a lignin, e.g., a natural or synthetically modified lignin.
- the fiber source used to make the fibrous material already includes a binder so that no additional binder needs to be added to effect densification.
- the binder can serve other functions in addition to binding the fibrous material.
- the binder can act as a compatibility or coupling aid, helping to compatibilize the resin of the composite and the fibrous material.
- Specific examples of such binders include modified polymers that have been functionalized, e.g., with maleic anhydride.
- Maleic anhydride grafted polymers are available from DuPontTM under the tradename FUSABOND®.
- Other specific examples include modified ethylene acrylate carbon monoxide terpolymers and ethylene vinyl acetates (EVAs), also available from DuPontTM.
- the binder can include a fragrance or a scent.
- a suitable amount of binder added to the fibrous material, calculated on a dry weight basis, is, e.g., from about 0.01 percent to about 50 percent, e.g., 0.03 percent, 0.05 percent, 0.1 percent, 0.25 percent, 0.5 percent, 1.0 percent, 5 percent, 10 percent or more, e.g., 25 percent, based on a total weight of the densified fibrous material.
- the binder can be added to the fibrous material as a neat, pure liquid, as a liquid having the binder dissolved therein, as a dry powder of the binder, or as pellets of the binder.
- the amount of binder added to the fibrous material is greater than 50 percent (calculated on a dry weight basis), e.g., greater than 55 percent, greater than 60 percent, greater than 65 percent, greater than 75 percent, or even greater than 85 percent.
- these embodiments may have, e.g., less than 90 percent polymer (e.g., a thermoplastic polymer).
- the fibrous material after densification, can be in the form of pellets ( FIG. 20 ) or chips having a variety of shapes, the desired shape is, in part, dependent upon the application.
- the pellets or chips when the pellets or chips are to be dry blended with a resin, and then the blend plasticized and molded to form composite parts, it is often convenient for the pellets or chips to be cylindrical in shape, e.g., having a maximum transverse dimension of, e.g., 1 mm or more, e.g., 2 mm, 3 mm, 5 mm, 8 mm, 10 mm, 15 mm or more, e.g., 25 mm.
- Another convenient shape for making composites includes pellets or chips that are plate-like in form, e.g., having a thickness of 1 mm or more, e.g., 2 mm, 3 mm, 5 mm, 8 mm, 10 mm or more, e.g., 25 mm; a width of, e.g., 5 mm or more, e.g., 10 mm, 15 mm, 25 mm, 30 mm or more, e.g., 50 mm; and a length of 5 mm or more, e.g., 10 mm, 15 mm, 25 mm, 30 mm or more, e.g., 50 mm.
- the pellets can be made by extrusion through a die having a solid central portion such that the corresponding pellet has a hollow inside.
- the hollow can be generally in-line with the center of the pellet ( FIG. 20A ), or out of line with the center of the pellet ( FIG. 20B ).
- Making the pellet hollow inside can decrease the cooling time needed to fully set up the pellet, and can, therefore, increase the speed of the pellet formation.
- Each pellet can be the same or different transverse cross-section.
- the pellet can have, e.g., a transverse shape that is multi-lobal, e.g., tri-lobal as shown, or tetra-lobal, penta-lobal, hexa-lobal or deca-lobal. Making the pellets in such transverse shapes can decrease cooling time.
- a transverse shape that is multi-lobal, e.g., tri-lobal as shown, or tetra-lobal, penta-lobal, hexa-lobal or deca-lobal. Making the pellets in such transverse shapes can decrease cooling time.
- the pellets can be used, e.g., to form composites.
- the pellets or chips can also be used as themselves, e.g., as absorbents or controlled release matrices.
- controlled release matrices the pellets or chips can be used, e.g., to fertilize grass, to release drugs or biocides, or to release fragrances.
- absorbents the pellets or chips can be used, e.g., as pet bedding, packaging material or in pollution control systems.
- the pellets or chips can include a polymer, e.g., a degradable material.
- degradable polymers include polyhydroxy acids, e.g., polylactides, polyglycolides and copolymers of lactic acid and glycolic acid, poly(hydroxybutyric acid), poly(hydroxyvaleric acid), poly[lactide-co-( ⁇ -caprolactone)], poly[glycolide-co-( ⁇ -caprolactone)], polycarbonates, poly(amino acids), poly(hydroxyalkanoate)s, polyanhydrides, polyorthoesters and blends of these polymers.
- polyhydroxy acids e.g., polylactides, polyglycolides and copolymers of lactic acid and glycolic acid, poly(hydroxybutyric acid), poly(hydroxyvaleric acid), poly[lactide-co-( ⁇ -caprolactone)], poly[glycolide-co-( ⁇ -caprolactone)], polycarbonates, poly(amino acids), poly(hydroxyalkanoate)s, polyanhydrides, polyorthoesters and blends of these
- the densified fibrous material can be used to form articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, frames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes and crutches.
- articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs
- the pellets or chips have a variety of densities, the desired density, in part, depending upon the application.
- the pellets or chips can have, e.g., a density of about 0.11 g/cm 3 , 0.15 g/cm 3 , 0.20 g/cm 3 , 0.25 g/cm 3 , 0.3 g/cm 3 , 0.4 g/cm 3 , 0.5 g/cm 3 , 0.6 g/cm 3 , or more, e.g., 0.8 g/cm 3 .
- the densified fibrous material can be substituted for fibrous material since the densified fibrous material is converted back into a fibrous material inside a processing device, e.g., an extruder or an injection molding machine.
- a fibrous material having a low bulk density can be revertibly densified without using a binder to a fibrous material having a higher bulk density.
- a fibrous material having a bulk density of 0.05 g/cm 3 can be densified by sealing the fibrous material in a relatively air impermeable bag, and then evacuating air from the bag.
- the fibrous material can have, e.g., a bulk density of greater than 0.3 g/cm 3 , e.g., 0.5 g/cm 3 , 0.6 g/cm 3 , 0.7 g/cm 3 or more, e.g., 0.85 g/cm 3 .
- This can be advantageous when it is desirable to transport the fibrous material to another location, e.g., a remote manufacturing plant, prior to densification of the fibrous material with a binder.
- the densified fibrous material After piercing the air impermeable bag, the densified fibrous material reverts to nearly its initial bulk density, e.g., greater than 60 percent of its initial bulk density, e.g., 70 percent, 80 percent, 85 percent or more, e.g., 95 percent of its initial bulk density.
- an anti-static agent can be added to the fibrous material.
- a chemical anti-static compound e.g., a cationic compound, e.g., quaternary ammonium compound, can be added to the fibrous material.
- Static in the fibrous material can also be reduced, e.g., by induction, grounding or by ionization.
- FIG. 22 explains operation of a fibrous material generating and treating device 70 .
- Paper sheet 73 e.g., scrap bleached Kraft paper sheet
- a fiberizing apparatus 74 such as a rotary shearer.
- the sheet 73 is converted into fibrous material 12 ′ and is delivered to a fiber-loading zone 80 by conveyer 78 .
- the fibers of the fibrous material may be separated, e.g., by screening, into fractions having different L/D ratios.
- the fibrous material 12 ′ is delivered continuously to zone 80 , and in other embodiments, the fibrous material is delivered in batches.
- a blower 82 in loop 84 is positioned adjacent to the fiber-loading zone 80 and is capable of moving a gaseous medium, e.g., air, at a velocity and volume sufficient to circulate the fibrous material 12 ′ in a direction indicated by arrow 88 through loop 84 .
- a gaseous medium e.g., air
- the velocity of air traveling in the loop is sufficient to uniformly disperse and transport the fibrous material around the entire loop 84 .
- the velocity of flow is greater than 2,500 feet/minute, e.g., 5,000 feet/minute, 6,000 feet/minute or more, e.g., 7,500 feet/minute.
- binder application zone 90 which forms part of loop 84 , where binder is applied.
- binder application zone 90 applies a liquid binder solution 96 to the circulating fibrous material via nozzles 98 , 99 and 100 .
- the nozzles produce an atomized spray or mist of binder material, which impacts and coat the fibers as the fibers pass in proximity to the nozzles.
- Valve 102 is operated to control the flow of liquid binder material to the respective nozzles 98 , 99 , and 100 . After a desired quantity of binder material is applied, the valve 102 is closed.
- the binder application zone 90 is two to one hundred feet long or more, e.g., 125 feet, 150 feet, 250 feet long or more, e.g., 500 feet long. Longer binder application zones allow for application of binder over a longer period of time during passage of fibrous material 12 ′ through application zone 90 . In some embodiments, the nozzles are spaced apart from about three to about four feet along the length of loop 84 .
- the binder provides a coating over a substantial majority of the surface area of each fiber of the fibrous material 12 ′, e.g., fifty percent or more, e.g., sixty percent, seventy percent, seventy five percent or more, e.g., eighty percent. In some embodiments, the binder forms a coating which is about 1 micron thick or less, e.g., 0.5, 0.3 micron or less, e.g., 0.1 micron.
- any of the additives and/or fillers described herein can optionally be added to the loop 84 from a supply 106 during circulation of fibrous material 12 ′ to form a blend of fibers and additives.
- the coated fibrous material 110 is removed from loop 84 via a separator 112 , which is selectively connected to loop 84 by section 114 and gate valve 116 .
- valve 116 When valve 116 is opened, another valve 120 is also opened to allow air to enter the loop 84 to compensate for air exiting through separator 112 .
- separator 112 With separator 112 in the loop, the coated fibrous material is collected in separator 112 , and then removed from the separator by outlet 122 .
- the fibrous material is dried with an optional heater 130 before the material is removed from loop 84 .
- heated air may be blended with the air flowing through the conduit to accelerate the drying off the liquid, e.g., water, in which the binder is incorporated.
- the coated fibrous material is transferred from outlet 122 loosely onto a conveyor 132 where it is transferred to densification station 150 shown in FIG. 23 or densification station 200 shown in FIG. 24 .
- the coated fibrous material 110 from above is delivered from a headbox 152 through a slit 154 and onto a screen 156 , e.g., a Fourdrinier screen. Excess water is drawn away from the coated fibrous material 110 deposited on screen 156 by a conventional vacuum system under the screen (not shown), leaving a deposited undensified fibrous material 160 that includes the binder.
- the undensified fibrous 160 material is then transferred to two sets of calendar rolls 162 , 164 , each defining a respective nip through which the fibrous material passes. After passing through the nips, the undried densified material 170 enters a drying section 180 where it is dried, and then is chopped into pellet or chip form.
- the densified fibrous material can be made in a pellet mill.
- a pellet mill 200 has a hopper 201 for holding the undensified fibrous material 110 .
- the hopper 201 communicates with an auger 204 that is driven by variable speed motor 206 so that undensified fibrous material 110 can be transported to a conditioner 210 that stirs the undensified material 110 with paddles 212 that are rotated by conditioner motor 214 .
- Other ingredients e.g., any of the additives and/or fillers described herein, can be added at inlet 220 . If desired, heat may be added while the fibrous material is in conditioner 210 .
- the fibrous material passes from the conditioner 210 through a dump chute 222 , and to another auger 224 .
- the dump chute 222 as controlled by actuator 223 , allows for unobstructed passage of the fibrous material from conditioner 210 to auger 224 .
- Auger 224 is rotated by motor 230 , and controls the feeding of the fibrous material into die and roller assembly 232 .
- the fibrous material is introduced into a hollow, cylindrical die 240 which rotates about a horizontal axis and which has radially extending die holes 250 .
- Die 240 is rotated about the axis by motor 242 , which includes a horsepower gauge, indicating total power consumed by the motor 242 .
- a set of rollers 256 roll about the inner circumference of die 240 , around axes parallel to that of die 240 , to press the fibrous material through the die holes 250 , forming pellets 300 , which fall from chute 301 and which are captured and boxed.
- an apparatus 310 can be used to form a densified fibrous material 311 , e.g., a composite, e.g., a pressboard.
- the densified fibrous material 311 is formed from a fibrous material-binder combination 313 by laminating the fibrous material-binder combination 313 between members 312 and 314 . Laminating is accomplished, e.g., by applying pressure alone or by applying heat and pressure to an uncompressed composite 322 .
- the fibrous material-binder combination 313 can optionally include any of the additives discussed above.
- Apparatus 310 includes first and second members 312 and 314 provided from rolls 321 and 323 , respectively, and a hopper 320 for holding the fibrous material, binder and any additives.
- the fibrous material, binder and any additives are delivered between members 312 and 314 to form an uncompressed composite 322 .
- the uncompressed composite 322 is then passed through a series of heated rolls 330 , 332 , 334 , 336 , 338 , 340 and 342 that define a serpentine pathway, and then through nip rolls 350 , 352 and 354 , 356 to produce composite 311 .
- Agitators can be provided within hopper 320 to ensure that the fibrous material, binder and any additives do not clog or foul the feeding operation.
- the uncompressed composite 322 is partially densified after passing through the serpentine pathway defined by heated rolls 330 , 332 , 334 , 336 , 338 and 340 , and then is fully densified to form composite 311 by passing through nip rolls 350 , 352 and 354 , 356 .
- the fiber source used to make the fibrous material already includes a binder.
- no additional binder needs to be added to effect densification.
- the fibrous material is densified without the addition of a separate binder, e.g., a low glass transition temperature polymer.
- Nip rolls 354 , 356 can be rotated so that each has a surface speed greater than each nip roll 350 , 352 .
- the densified fibrous material is stretched between nip rolls 350 , 352 and nip rolls 354 , 356 .
- stretching the densified fibrous material is desirable because stretching can improve many mechanical properties of the composite, e.g., flexural modulus, bend resistance and tensile strength.
- the members e.g., webs
- the members can be made of, e.g., polycoated paper, plastic film, plastic stock or a textile scrim material, e.g., a woven or non-woven textile scrim material.
- a thickness T 1 and T 2 of members 312 and 314 can be, e.g., less than 0.050 inch, e.g., 0.040 inch, 0.025 inch, 0.020 inch, 0.010 inch, 0.005 inch or less, e.g., 0.0025 inch.
- the thickness T 1 and T 2 of members 312 and 314 can be greater than 0.050 inch, e.g., 0.060 inch, 0.065 inch, 0.075 inch, 0.085 inch, 0.100 inch, 0.150 inch, 0.250 inch, 0.75 inch or more, e.g., 2.00 inch.
- the rolls 330 , 332 , 334 , 336 , 338 and 340 are heated to between 300° F. to about 500° F. In embodiments in which plastic film is used as a member material, these temperatures act to quickly soften the polymeric material of the film.
- heated rolls 330 , 332 , 334 , 336 , 338 and 340 are between about 5 inches in diameter to about 42 inches in diameter, e.g., 10 inches, 15 inches, 20 inches, 25 inches or larger, e.g., 36 inches.
- the member feed rate can be, e.g., between about 3.5 feet per minute to about 250 feet per minute, e.g., 25 feet per minute, 50 feet per minute, 100 feet per minute or higher, e.g., 175 feet per minute.
- Nip rolls 350 , 352 and 354 , 356 can be heated or unheated. When heated, they are typically heated to a temperature less than heated rolls 330 , 332 , 334 , 336 , 338 and 340 to allow the materials that will form the densified fibrous material to begin to cool and set. For example, nip rolls 350 , 352 and 354 , 356 are heated to between 100° F. to about 300° F. Pressure between the nip rolls is, e.g., at least about 500 pounds per linear inch, e.g., 1,000 pounds per linear inch, 2,500 pounds per linear inch, 5,000 pounds per linear inch or more, e.g., 25,000 pounds per linear inch.
- a thickness T′ of the densified fibrous material 311 is at least about two times less than a thickness T of the uncompressed composite 322 , e.g., three times, four times, five times or less, e.g., ten times less. Accordingly, the bulk density of the densified fibrous material is greater than the uncompressed composite.
- the density of the uncompressed composite can be, e.g., less than 0.25 g/cm 3 , e.g., 0.20 g/cm 3 , 0.15 g/cm 3 , 0.10 g/cm 3 , 0.05 g/cm 3 or less, e.g., 0.025 g/cm 3
- the bulk density of the densified fibrous material can be, e.g., greater than about 0.3 g/cm 3 , e.g., 0.4 g/cm 3 , 0.5 g/cm 3 , 0.6 g/cm 3 , or more, e.g., 0.8 g/cm 3 .
- Cooled densified fibrous material 311 can be rolled up or cut into sheets. Densifying a fibrous material between members can be advantageous when it is desirable to transport the fibrous material to another location, e.g., a remote manufacturing plant. After reaching the other location, the densified fibrous material can be re-converted into a fibrous material by any of the methods discussed herein.
- cooled densified fibrous material can be used in a variety of applications. For example, it can be used for sound-proofing, insulation, structural members, high strength boxes, and partition walls.
- a binder is applied to a fibrous material by spraying a binder solution, e.g., a binder solution containing the binder dissolved in water, onto the fibrous material
- a binder solution e.g., a binder solution containing the binder dissolved in water
- the binder is applied to the fibrous material as neat liquid of the binder or as a dry powder.
- the binder can also be applied as a gaseous material.
- the densified fibrous material is first collected in a roll.
- the densified fibrous web can be used, e.g., as an absorbent mat material, or it can be transported to a remote manufacturing site where it is converted into pellets or chips.
- the densified fibrous web material can be a convenient form in which to transport the fibrous material because of its higher bulk density.
- single layer members 312 and 314 are used to form a densified fibrous material 311 , e.g., a composite
- multilayer members are used.
- members can each have, e.g., two layers, three layers, five layers or more, e.g., seven layers.
- densified fibrous materials have been described in which fibrous material is sandwiched between two members, in some embodiments, a densified fibrous material is made by compressing a fibrous material that is under a single member.
- Fibrous material was prepared according to Example 2. Approximately 1 lb of water was sprayed onto each 10 lb of fibrous material. The fibrous material was densified using a California Pellet Mill 1100 operating at 75° C. Pellets were obtained having a bulk density ranging from about 7 lb/ft 3 to about 15 lb/ft 3 .
- Fibrous material was prepared according to Example 2.
- Composites including any of the above discussed fibrous materials (including the densified fibrous materials) or blends of any of the above fibrous materials, e.g., the first 12 or second fibrous material 14 , and a resin, e.g., a thermoplastic resin or a thermosetting resin, can be prepared by combining the desired fibrous material and the desired resin.
- the desired fibrous material can be combined with the desired resin, e.g., by mixing the fibrous material and the resin in an extruder or other mixer.
- the fibrous material can be combined with the resin as the fibrous material itself or as a densified fibrous material that can be re-opened during the combining.
- thermoplastic resins include rigid and elastomeric thermoplastics.
- Rigid thermoplastics include polyolefins (e.g., polyethylene, polypropylene, or polyolefin copolymers), polyesters (e.g., polyethylene terephthalate), polyamides (e.g., nylon 6, 6/12 or 6/10), and polyethyleneimines.
- elastomeric thermoplastic resins include elastomeric styrenic copolymers (e.g., styrene-ethylene-butylene-styrene copolymers), polyamide elastomers (e.g., polyether-polyamide copolymers) and ethylene-vinyl acetate copolymer.
- the thermoplastic resin has a melt flow rate of between 10 g/10 minutes to 60 g/1 minutes, e.g., between 20 g/10 minutes to 50 g/10 minutes, or between 30 g/10 minutes to 45 g/10 minutes, as measured using ASTM 1238.
- compatible blends of any of the above thermoplastic resins can be used.
- the thermoplastic resin has a polydispersity index (PDI), i.e., a ratio of the weight average molecular weight to the number average molecular weight, of greater than 1.5, e.g., greater than 2.0, greater than 2.5, greater than 5.0, greater than 7.5, or even greater than 10.0.
- PDI polydispersity index
- polyolefins or blends of polyolefins are utilized as the thermoplastic resin.
- thermosetting resins examples include natural rubber, butadiene-rubber and polyurethanes.
- the fibers of the fibrous materials can have a relatively large average length-to-diameter ratio (e.g., greater than 20-to-1), even if they have been sheared more than once.
- the fibers of the fibrous materials described herein may have a relatively narrow length and/or length-to-diameter ratio distribution.
- the relatively large average length-to-diameter ratio and the relatively narrow length and/or length-to-diameter ratio distribution are, at least in part, responsible for the ease at which the fibrous materials are dispersed in a resin, e.g., a molten thermoplastic resin.
- the relatively large average length-to-diameter ratio and the relatively narrow length and/or length-to-diameter ratio distribution are, at least in part, responsible for the consistent properties of the fibrous materials, the predictable rheology modification the fibrous materials impart on a resin, the ease at which the combinations of the fibrous materials and resins are cast, extruded and injection molded, the ease in which the fibrous materials pass through small, often torturous channels and openings, and the excellent surface finishes possible with molded parts, e.g., glossy finishes and/or finishes substantially devoid of visible speckles, when this is desired.
- a chemical foaming agent e.g., an endothermic or exothermic foaming agent
- a gas e.g., nitrogen or carbon dioxide
- Chemical foaming agent are available from Clariant Corporation, e.g., under the tradename HYDROCEROL®.
- Additives can be added, e.g., to the combination of a fibrous material and resin.
- Additives include fillers such as calcium carbonate, graphite, wollastonite, mica, glass, fiber glass, silica, and talc; inorganic flame retardants such as alumina trihydrate or magnesium hydroxide; organic flame retardants such as chlorinated or brominated organic compounds; ground construction waste; ground tire rubber; carbon fibers; or metal fibers or powders (e.g., aluminum, stainless steel).
- additives can reinforce, extend, or change electrical, mechanical or compatibility properties.
- Other additives include lignin, fragrances, coupling agents, compatibilizers, e.g., maleated polypropylene, processing aids, lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opacifiers, heat stabilizers, colorants, foaming agents, impact modifiers, polymers, e.g., degradable polymers, photostabilizers, biocides, antistatic agents, e.g., stearates or ethoxylated fatty acid amines.
- compatibilizers e.g., maleated polypropylene
- processing aids e.g., lubricants, e.g., fluorinated polyethylene, plasticizers, antioxidants, opacifiers, heat stabilizers, colorants, foaming agents, impact modifiers, polymers, e.g., degradable polymers, photostabilizers, biocides
- Suitable antistatic compounds include conductive carbon blacks, carbon fibers, metal fillers, cationic compounds, e.g., quaternary ammonium compounds, e.g., N-(3-chloro-2-hydroxypropyl)-trimethylammonium chloride, alkanolamides, and amines.
- cationic compounds e.g., quaternary ammonium compounds, e.g., N-(3-chloro-2-hydroxypropyl)-trimethylammonium chloride, alkanolamides, and amines.
- degradable polymers include polyhydroxy acids, e.g., polylactides, polyglycolides and copolymers of lactic acid and glycolic acid, poly(hydroxybutyric acid), poly(hydroxyvaleric acid), poly[lactide-co-(e-caprolactone)], poly[glycolide-co-(e-caprolactone)], polycarbonates, poly(amino acids), poly(hydroxyalkanoate)s, polyanhydrides, polyorthoesters and blends of these polymers.
- polyhydroxy acids e.g., polylactides, polyglycolides and copolymers of lactic acid and glycolic acid, poly(hydroxybutyric acid), poly(hydroxyvaleric acid), poly[lactide-co-(e-caprolactone)], poly[glycolide-co-(e-caprolactone)], polycarbonates, poly(amino acids), poly(hydroxyalkanoate)s, polyanhydrides, polyorthoesters and blends of these
- additives When described additives are included, they can be present in amounts, calculated on a dry weight basis, of from below 1 percent to as high as 80 percent, based on total weight of the fibrous material. More typically, amounts range from between about 0.5 percent to about 50 percent by weight, e.g., 5 percent, 10 percent, 20 percent, 30, percent or more, e.g., 40 percent.
- any additives described herein can be encapsulated, e.g., spray dried or microencapsulated, e.g., to protect the additives from heat or moisture during handling.
- the fibrous materials, densified fibrous materials, resins or additives may be dyed.
- the fibrous material can be dyed before combining with the resin and compounding to form composites.
- this dyeing can be helpful in masking or hiding the fibrous material, especially large agglomerations of the fibrous material, in molded or extruded parts, when this is desired.
- Such large agglomerations when present in relatively high concentrations, can show up as speckles in the surfaces of the molded or extruded parts.
- the desired fibrous material can be dyed using an acid dye, direct dye or a reactive dye.
- dyes are available from Spectra Dyes, Kearny, N.J. or Keystone Aniline Corporation, Chicago, Ill.
- Specific examples of dyes include SPECTRATM LIGHT YELLOW 2G, SPECTRACIDTM YELLOW 4GL CONC 200, SPECTRANYLTM RHODAMINE 8, SPECTRANYLTM NEUTRAL RED B, SPECTRAMINETM BENZOPERPURINE, SPECTRADIAZOTM BLACK OB, SPECTRAMINETM TURQUOISE G, and SPECTRAMINETM GREY LVL 200%, each being available from Spectra Dyes.
- resin color concentrates containing pigments are blended with dyes. When such blends are then compounded with the desired fibrous material, the fibrous material may be dyed in-situ during the compounding. Color concentrates are available from Clariant.
- the fragrance e.g., natural wood fragrance
- the fragrance can be compounded into the resin used to make the composite.
- the fragrance is compounded directly into the resin as an oil.
- the oil can be compounded into the resin using a roll mill, e.g., a Banbury® mixer or an extruder, e.g., a twin-screw extruder with counter-rotating screws.
- a Banbury® mixer is the F-Series Banbury® mixer, manufactured by Farrel.
- twin-screw extruder is the WP ZSK 50 MEGAcompounderTM, manufactured by Krupp Werner & Pfleiderer.
- the scented resin can be added to the fibrous material and extruded or molded.
- master batches of fragrance-filled resins are available commercially from International Flavors and Fragrances, under the tradename PolylffTM or from the RTP Company.
- the amount of fragrance in the composite is between about 0.005% by weight and about 10% by weight, e.g., between about 0.1% and about 5% or 0.25% and about 2.5%.
- fragrances include evergreen or redwood.
- Other fragrances include peppermint, cherry, strawberry, peach, lime, spearmint, cinnamon, anise, basil, bergamot, black pepper, camphor, chamomile, citronella, eucalyptus, pine, fir, geranium, ginger, grapefruit, jasmine, juniperberry, lavender, lemon, mandarin, marjoram, musk, myrrh, orange, patchouli, rose, rosemary, sage, sandalwood, tea tree, thyme, wintergreen, ylang ylang, vanilla, new car or mixtures of these fragrances.
- the amount of fragrance in the fibrous material-fragrance combination is between about 0.005% by weight and about 20% by weight, e.g., between about 0.1% and about 5% or 0.25% and about 2.5%.
- inorganic fillers such as calcium carbonate (e.g., precipitated calcium carbonate or natural calcium carbonate), aragonite clay, orthorhombic clays, calcite clay, rhombohedral clays, kaolin, clay, bentonite clay, dicalcium phosphate, tricalcium phosphate, calcium pyrophosphate, insoluble sodium metaphosphate, precipitated calcium carbonate, magnesium orthophosphate, trimagnesium phosphate, hydroxyapatites, synthetic apatites, alumina, silica xerogel, metal aluminosilicate complexes, sodium aluminum silicates, zirconium silicate, silicon dioxide or combinations of the inorganic additives may be used.
- the fillers can have, e.g., a particle size of greater than 1 micron, e.g., greater than 2
- Nanometer scale fillers can also be used alone, or in combination with fibrous materials.
- the fillers can be in the form of, e.g., a particle, a plate or a fiber.
- nanometer sized clays, silicon and carbon nanotubes, and silicon and carbon nanowires can be used.
- the filler can have a transverse dimension less than 1000 nm, e.g., less than 900 nm, 800 nm, 750 nm, 600 nm, 500 nm, 350 nm, 300 nm, 250 nm, 200 nm, less than 100 nm, or even less than 50 nm.
- the nano-clay is a montmorillonite.
- montmorillonite Such clays are available from Nanocor, Inc. and Southern Clay products, and have been described in U.S. Pat. Nos. 6,849,680 and 6,737,464.
- the clays can be surface treated before mixing into, e.g., a resin or a fibrous material.
- the clay can be surface is treated so that its surface is ionic in nature, e.g., cationic or anionic.
- Aggregated or agglomerated nanometer scale fillers, or nanometer scale fillers that are assembled into supramolecular structures, e.g., self-assembled supramolecular structures can also be used.
- the aggregated or supramolecular fillers can be open or closed in structure, and can have a variety of shapes, e.g., cage, tube or spherical.
- Any composite described herein can be in the form of articles such as pipes, panels, decking materials, boards, housings, sheets, blocks, bricks, poles, fencing, members, doors, shutters, awnings, shades, signs, frames, window casings, backboards, flooring, tiles, railroad ties, trays, tool handles, stalls, films, wraps, tapes, boxes, baskets, racks, casings, binders, dividers, walls, mats, flames, bookcases, sculptures, chairs, tables, desks, toys, games, pallets, wharves, piers, boats, masts, septic tanks, automotive panels, computer housings, above- and below-ground electrical casings, furniture, picnic tables, benches, shelters, trays, hangers, servers, caskets, book covers, canes, crutches, house wares and structures.
- radiation cross-linked composites can be made, e.g., by combining a fibrous material that includes discrete fibers with a radiation cross-linkable resin, e.g., a thermoplastic resin (e.g., a high melt flow rate polypropylene) to provide a fibrous material/cross-linkable resin combination.
- a radiation cross-linkable resin e.g., a thermoplastic resin (e.g., a high melt flow rate polypropylene)
- the fibrous material can have, e.g., an average length-to-diameter ratio of greater than 5, and a standard deviation of a fiber length that is, e.g., less than eighty five percent of an average fiber length.
- the fibrous material/cross-linkable resin is formed, e.g., using extrusion or injection molding, into a desired shape, e.g., a decking board, and is irradiated, e.g., with an ionizing radiation (e.g., an electron beam, x-ray radiation or gamma radiation) to at least partially cross-link the cross-linkable resin.
- an ionizing radiation e.g., an electron beam, x-ray radiation or gamma radiation
- a gamma irradiator 400 includes gamma radiation sources 408 , e.g., 60 Co pellets, a working table 410 for holding the composite to be irradiated and storage 412 , e.g., made of a plurality iron plates, all of which are housed in a concrete containment chamber 402 that includes a maze entranceway 404 beyond a lead-lined door 406 .
- Storage 412 includes a plurality of channels 420 , e.g., sixteen or more channels, allowing the gamma radiation sources 408 to pass through storage 412 on their way proximate the working table 410 .
- the composite to be irradiated is placed on working table 410 .
- the irradiator is configured to deliver the desired dose rate and monitoring equipment is connected to experimental block 440 .
- the operator then leaves the containment chamber 402 , passing through the maze entranceway 404 and through the lead-lined door 406 .
- the operator mans a control panel 442 , instructing a computer to lift the radiation sources 408 into working position using cylinder 441 attached to a hydraulic pump 444 .
- the electromagnetic radiation can have, e.g., energy per photon (in electron volts) of greater than 10 2 eV, e.g., greater than 10 3 , 10 4 , 10 5 , 10 6 , or even greater than 10 7 eV. In some embodiments, the electromagnetic radiation has energy per photon of between 10 4 and 10 7 , e.g., between 10 5 and 10 6 eV.
- the electromagnetic radiation can have a frequency of, e.g., greater than 10 16 hz, greater than 10 17 hz, 10 18 , 10 19 , 10 20 , or even greater than 10 21 hz. In some embodiments, the electromagnetic radiation has a frequency of between 10 18 and 10 22 hz, e.g., between 10 19 to 10 21 hz.
- Electron beams can be generated, e.g., by electrostatic generators, cascade generators, transformer generators, low energy accelerators with a scanning system, low energy accelerators with a linear cathode, linear accelerators, and pulsed accelerators. Electrons as an ionizing radiation source can be useful, e.g., for composites having relatively thin cross-sections, e.g., less than 0.5 inch, e.g., less than 0.4 inch, 0.3 inch, 0.2 inch, or less than 0.1 inch.
- the energy of each electron of the electron beam is from about 0.3 MeV to about 2.0 MeV (million electron volts), e.g., from about 0.5 MeV to about 1.5 MeV, or from about 0.7 MeV to about 1.25 MeV.
- the irradiating (with any radiation source) is performed until the fibrous material/cross-linkable resin combination receives a dose of at least 0.25 Mrad, e.g., at least 1.0 Mrad, at least 2.5 Mrad, at least 5.0 Mrad, or at least 10.0 Mrad. In some embodiments, the irradiating is performed until the fibrous material/cross-linkable resin combination receives a dose of between 1.0 Mrad and 6.0 Mrad, e.g., between 1.5 Mrad and 4.0 Mrad.
- the irradiating is performed at a dose rate of between 5.0 and 1500.0 kilorads/hour, e.g., between 10.0 and 750.0 kilorads/hour or between 50.0 and 350.0 kilorads/hours.
- the radiation cross-linkable resin can be, e.g., a thermoplastic or a thermoset (e.g., a cast thermoset).
- the radiation cross-linkable resin can be a polyolefin, e.g., a polyethylene (e.g., a copolymer of polyethylene), a polypropylene (e.g., a copolymer of polypropylene), a polyester (e.g., polyethylene terephthalate), a polyamide (e.g., nylon 6, 6/12 or 6/10), a polyethyleneimine, elastomeric styrenic copolymers (e.g., styrene-ethylene-butylene-styrene copolymers), a polyamide elastomer (e.g., polyether-polyamide copolymer), ethylene-vinyl acetate copolymer, cast polyurethane, cast silicone, or compatible mixtures of these resins.
- the resin is a polyolefin that has a polydispersity of greater than 2.0, e.g., greater than 3.0, greater than 3.5, greater than 4.0, greater than 4.5, greater than 5.0, greater than 7.5 or even greater than 10.0 (measured using high temperature gel permeation chromatography against polystyrene standards; see, e.g., ASTM D6474-99).
- a high polydispersity can improve impact resistance in the cross-linked composite.
- the polyolefin has a melt flow rate greater than 10.0 g/10 minutes, e.g., greater than 15.0, greater than 20.0, greater than 25.0, greater than 30.0, or even greater than 50.0 g/10 minutes (measured using ASTM D1238, 230° C./2.16 kg).
- a high melt flow can aid in the production of the composite, e.g., by reducing shear heating during the forming of the composite.
- the resin is a 50:50 weight percent blend of 20 melt flow rate (MFR) polypropylene and 50 MFR polypropylene.
- MFR melt flow rate
- Polypropylenes are available from Sunoco Chemical.
- the crosslinked composites can include any or any combination of the fillers and/or additive disclosed herein.
- FIG. 27 illustrates a “dry” containment system
- water containment systems are possible.
- the embodiment of FIG. 27 illustrates irradiation of a composite under ambient conditions, the composite can be cooled during the irradiation.
- the embodiment of FIG. 27 illustrates irradiation in normal atmospheric air, irradiation can take place in an inert atmosphere, e.g., nitrogen or argon atmosphere.
- a composite 500 e.g., in the form of a step stool (as shown), includes a resin and a fibrous material 504 and has an external surface 505 . Some of the fibrous material is visible on, in, or just beneath the external surface of the composite. Such composites can have unique, pleasing or even striking visual properties, and at the same time can have desirable mechanical properties, e.g., flexural strength and impact resistance.
- the composite can be made, e.g., by combining a resin and a fibrous material 14 to provide a resin/fibrous material combination, and compressing the resin/fibrous material combination to provide the composite having the external surface.
- the resin, the fibrous material and the conditions for forming the composite are chosen such that fibrous material is visible in, on or just beneath the external surface, rather than being deeply buried below the surface where it would not be visible.
- fibrous material is visible beneath the exterior surface of the composite when the fibrous material is under the exterior surface, e.g., a distance of less than 0.100 inch, e.g., less than 0.050 inch, less than 0.025 inch, less than 0.010 inch, less than 0.005 inch, less than 0.0025 inch, or a distance of less than 0.001 inch.
- the composites can be made using any plastic processing machinery, e.g., injection molding equipment and compression molding equipment or extrusion equipment.
- the resin can be a thermoplastic or a thermoset.
- the resin can be, e.g., a polyolefin, such as a polyethylene (e.g., a copolymer of polyethylene), or a polypropylene (e.g., a copolymer of polypropylene); a polyester, such as polyethylene terephthalate (PET); a polyamide, such as nylon 6, 6/12 or 6/10; an elastomeric styrenic copolymer, such as a styrene-ethylene-butylene-styrene copolymer; a polyamide elastomers, such as polyether-polyamide copolymer; an ethylene-vinyl acetate copolymer; or mixtures of these resin.
- a polyolefin such as a polyethylene (e.g., a copolymer of polyethylene), or a polypropylene (e.g., a copolymer of
- the resin is a polyolefin, e.g., a polypropylene, having a melt flow rate of less than 50 g/10 minutes, e.g., less than 25 grams/10 minutes, less than 20 grams/10 minutes, less than 17 g/10 minutes, less than 15 grams/10 minutes, less than 10 g/10 minutes, less than 7.5 grams/10 minutes, less than 5 g/10 minutes, less than 2.5 grams/10 minutes, or even less than 1 g/10 minutes.
- the lower limit of the melt flow will depend upon the processing technique used to form the composite, e.g., injection molding or extrusion. For injection molding, it can be desirable that the melt flow rate be greater than 0.5 grams/10 minutes.
- melt flow rate be greater than 0.1 grams/10 minutes.
- Melt flow rats are measured using ASTM D1238 at 230° C. and 2.16 kg, the disclosure of which is hereby incorporated by reference herein in its entirety.
- the fibrous material used can be, e.g., a densified fibrous material made by application of pressure to a fibrous material (optionally having a binder), e.g., by passing the fibrous material through a nip defined between counter-rotating pressure rolls or by passing the fibrous material through a pellet mill, as discussed above.
- the densified fibrous material can be, e.g., in the form of pellets or chips or other geometries having a variety of shapes.
- the density of the densified fibrous material can be, e.g., greater than 0.11 g/cm 3 , e.g., greater than 0.15 g/cm 3 , greater than 0.20 g/cm 3 , greater than 0.25 g/cm 3 , greater than 0.3 g/cm 3 , greater than 0.4 g/cm 3 , greater than 0.5 g/cm 3 , or even greater than 0.6 g/cm 3 . It is desirable to select a density such that the densified material “comes apart” under shear and/or heat to release the fibrous material or agglomerated fibrous material. Generally, it is desirable that the densified fibrous material have a density of less than 0.9 g/cm 3 .
- the fibers of the fibrous materials can have a relatively large average length-to-diameter ratio (e.g., greater than 20-to-1).
- the average length-to-diameter ratio of the second fibrous material 14 can be, e.g. greater than 10/1, e.g., greater than 25/1 or greater than 50/1.
- An average length of the second fibrous material 14 can be, e.g., between about 0.5 mm and 2.5 mm, e.g., between about 0.75 mm and 1.0 mm, and an average width (i.e., diameter) of the second fibrous material 14 can be, e.g., between about 5 ⁇ m and 50 ⁇ m, e.g., between about 10 ⁇ m and 30 ⁇ m.
- the fibrous materials have a relatively large percentage of fibers greater than 2.5 mm in length.
- at least 2.5 percent by weight of the fibrous material is fibers having a length greater than 2.5 mm, e.g., at least 5.0 percent by weight of the fibrous material is fibers having a length greater than 2.5 mm, at least 7.5 percent by weight of the fibrous material is fibers have a length greater than 2.5 mm, or at least 10.0 percent by weight of the fibrous is fibers having length greater than 2.5 mm.
- less than 25 percent by weight of the fibrous material is fibers having a length greater than 2.5 mm.
- the composite can have, e.g., greater than 20 percent by weight fibrous material, e.g., greater than 30 percent, greater than 40 percent, greater than 50 percent, greater than 55 percent or even greater than 60 by weight fibrous material.
- the composites generally have less than 70 percent by weight fibrous material.
- the fibrous material can be colored, e.g., to enhance the strength of the visual effect.
- the fibrous material can be colored, e.g., by dying, before combining with the resin and to form the composites. In some implementations, this dyeing can, e.g., enhance visibility of the fibrous material in the external surface, especially large agglomerations of fibrous material.
- the resin can be colored, e.g., with a pigment or dye, to enhance the contrast between the fibrous material (colored or natural) and the resin, e.g., to enhance the overall strength of the visual effect.
- Color concentrates are available from Clariant.
- any of these composites having certain visual attributes can include any of the additives described herein, including fragrances.
- the composite can be formed into a variety of shapes, such as those described above.
- “speckled” composites can be prepared by forming a composite 600 by compressing a molten resin against a mold 602 having a cooled surface 604 , and then demolding the formed composite 600 .
- the compressing is performed against a mold surface having a temperature of less than 100° C., e.g., less than 75° C., less than 50° C., less than 25° C., or less than 15° C.
- Still other composites having unique, pleasing or even striking visual properties and desirable mechanical properties include a transparent resin and a fibrous material.
- the fibrous material can be seen within the composite.
- a transparent resin and a fibrous material are combined to provide a transparent resin/fibrous material combination and the transparent resin/fibrous material combination is compressed, e.g., in an extruder or in an a mold, to provide the composite.
- the resin can be a thermoplastic or a thermoset.
- the resin can be, e.g., a clarified polyolefin, such as a clarified polypropylene (e.g., a polypropylene copolymer); a polyester, such as polyethylene terephthalate (PET); an amorphous polyamide; a polycarbonate; a styrenic polymer, such as styrene-acrylonitrile-copolymer (SAN); a polyacrylate, such as polymethylmethacrylate (PMMA).
- a clarified polyolefin such as a clarified polypropylene (e.g., a polypropylene copolymer)
- PET polyethylene terephthalate
- PET polyethylene terephthalate
- SAN styrenic polymer
- PMMA polyacrylate
- PMMA polymethylmethacrylate
- Clarifying agents for polyolefins are available from Milliken Chemical under the trade name MILLAD®, e.g., MILLAD® 3988. Clarified polyolefin colorants are also available from Milliken Chemical under the trade name CLEARTINT®.
- the resin have a spectral transmission of greater than 60 percent, e.g., greater than 65 percent, greater than 70 percent, greater than 75 percent, greater than 80 percent, greater than 85 percent, or even greater than 90 percent.
- the resin it is also often desirable for the resin to have a haze of less than 40 percent, e.g., less than 35 percent, less than 30 percent, less than 25 percent, less than 20 percent, less than 15 percent, or even less than 10 percent. Both spectral transmission and haze are measured using ASTM D1003-92, which is hereby incorporated by reference herein in its entirety.
- the composite have a relatively low content of fibrous material, e.g., less than about 20 percent by weight fibrous material, less than 17.5 percent, less than 15 percent, less than 12.5 percent, less than 10 percent, less than 7.5 percent, less than 5 percent, less than 2.5 percent, or even less than 1 percent by weight fibrous material.
- a relatively low fiber content allows light to pass through the composite so that masses of fibrous material can be seen inside the composite.
- a resin/fibrous material composite can have an inner portion 610 that includes a first resin that has substantially no fibrous material and an outer portion 612 that includes a second resin that surrounds the inner portion and that includes substantially all of the fibrous material.
- a composite can be made, e.g., by co-molding or co-extrusion. Any of the above described fibrous materials or additives can be used in preparing such a composite. Such composites can be formed in any of the shapes described above.
- the first and second materials can be the same or different, and can be, e.g., any of the resins described above.
- a transparent resin/fibrous material composite can have an inner portion 620 having a first resin and substantially all of the fibrous material and an outer portion 622 surrounding the inner portion having a second resin and having substantially no fibrous material.
- Any of the above described fibrous materials or additives can be used with used in preparing such a composite.
- Such composites can be formed in any of the shapes described above.
- the first and second materials can be the same or different, and can be, e.g., any of the resins described above.
Abstract
Description
Claims (15)
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Cited By (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8074910B2 (en) * | 2005-03-24 | 2011-12-13 | Xyleco, Inc. | Fibrous materials and composites |
WO2012170707A1 (en) | 2011-06-09 | 2012-12-13 | Xyleco Inc. | Processing biomass |
WO2013096693A1 (en) | 2011-12-22 | 2013-06-27 | Xyleco, Inc. | Production of sugar and alcohol from biomass |
WO2013096452A1 (en) | 2011-12-22 | 2013-06-27 | Xyleco, Inc. | Processing biomass for use in fuel cells |
WO2014059140A1 (en) | 2012-10-10 | 2014-04-17 | Xyleco, Inc. | Treating biomass |
US8778136B2 (en) | 2009-05-28 | 2014-07-15 | Gp Cellulose Gmbh | Modified cellulose from chemical kraft fiber and methods of making and using the same |
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US9512563B2 (en) | 2009-05-28 | 2016-12-06 | Gp Cellulose Gmbh | Surface treated modified cellulose from chemical kraft fiber and methods of making and using same |
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US9701838B2 (en) | 2014-03-21 | 2017-07-11 | Xyleco, Inc. | Method and structures for processing materials |
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US10501761B2 (en) | 2013-04-26 | 2019-12-10 | Xyleco, Inc. | Processing biomass to obtain hydroxylcarboxylic acids |
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US11015059B2 (en) | 2019-05-23 | 2021-05-25 | Bolt Threads, Inc. | Composite material, and methods for production thereof |
Families Citing this family (53)
Publication number | Priority date | Publication date | Assignee | Title |
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EA025362B1 (en) | 2006-10-26 | 2016-12-30 | Ксилеко, Инк. | Processing biomass |
DE102007058127A1 (en) * | 2007-11-30 | 2009-06-04 | Pallmann Maschinenfabrik Gmbh & Co Kg | Device for dissolving the composite of feedstock present in the composite |
US8236535B2 (en) | 2008-04-30 | 2012-08-07 | Xyleco, Inc. | Processing biomass |
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US8329455B2 (en) | 2011-07-08 | 2012-12-11 | Aikan North America, Inc. | Systems and methods for digestion of solid waste |
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CN112556976B (en) * | 2020-12-09 | 2022-08-12 | 中国航天空气动力技术研究院 | Speckle manufacturing method for deformation measurement of special wind tunnel experiment model |
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DE102021107363A1 (en) | 2021-03-24 | 2022-09-29 | Delcotex Delius Techtex Gmbh & Co. Kg | Textile fabric and its use as well as method for its production |
RU207852U1 (en) * | 2021-05-11 | 2021-11-19 | Общество с ограниченной ответственностью «К-СИСТЕМС ГРУПП» | Electrically Conductive Carbon Fiber Roll Material |
WO2022245658A1 (en) * | 2021-05-17 | 2022-11-24 | Reenano Llc | An apparatus and system for manufacturing nanocellulose compositions |
CN113334855A (en) * | 2021-05-31 | 2021-09-03 | 江阴市瑞和盛纸品有限公司 | Degradable edible powder composite paper lunch box and manufacturing process thereof |
WO2023147247A1 (en) * | 2022-01-31 | 2023-08-03 | Purdue Research Foundation | Production of rice straw fiber board using lignin from catalytically depolymerized rice straw |
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WO2023227745A1 (en) * | 2022-05-25 | 2023-11-30 | Plantics Holding B.V. | Method for manufacturing filler-containing compositions with a specific curing regimen |
Citations (279)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1057151A (en) * | 1911-08-31 | 1913-03-25 | Guy C Howard | Process for the production of mechanical wood-pulp. |
US1405944A (en) * | 1919-04-23 | 1922-02-07 | Shartle Continuous Beater Comp | Process of manufacturing paper pulp |
US1824221A (en) | 1928-10-24 | 1931-09-22 | Masonite Corp | Process and apparatus for disintegration of fibrous material |
US1897620A (en) * | 1932-01-15 | 1933-02-14 | Respats Inc | Continuous process of reducing or reforming wood or other fibrous material |
US2516847A (en) | 1944-12-01 | 1950-08-01 | Masonite Corp | Process of sizing exploded fibers |
US2519442A (en) | 1944-04-28 | 1950-08-22 | Saint Gobain | Compositions containing cellulosic filler united by polyvinyl chloride |
US2558378A (en) | 1947-01-15 | 1951-06-26 | Delaware Floor Products Inc | Composition for floor and wall covering comprising plasticized vinyl resin and filler and method of making same |
US2635976A (en) | 1948-06-15 | 1953-04-21 | Plywood Res Foundation | Method of making synthetic constructional boards and products thereof |
US2658828A (en) | 1948-09-15 | 1953-11-10 | Chemloch Corp | Process of combining synthetic resins and other materials with cellulose |
US2665261A (en) | 1950-05-12 | 1954-01-05 | Allied Chem & Dye Corp | Production of articles of high impact strength |
US2680102A (en) | 1952-07-03 | 1954-06-01 | Homasote Company | Fire-resistant product from comminuted woody material, urea, or melamine-formaldehyde, chlorinated hydrocarbon resin, and hydrated alumina |
US2757150A (en) | 1953-01-30 | 1956-07-31 | Weyerhaeuser Timber Co | Preparing hot-moldable thermosetting resin and cellulose fiber mixtures |
US2789903A (en) | 1954-09-02 | 1957-04-23 | Celanese Corp | Process for production of shaped articles comprising fibrous particles and a copolymer of vinyl acetate and an ethylenically unsaturated acid |
US2877953A (en) * | 1953-09-29 | 1959-03-17 | Weyerhaeuser Timber Co | Granular sclerenchyma and the method of its production from douglas fir bark |
US2935763A (en) | 1954-09-01 | 1960-05-10 | Us Rubber Co | Method of forming pellets of a synthetic rubber latex and a particulate resin |
US3308218A (en) | 1961-05-24 | 1967-03-07 | Wood Conversion Co | Method for producing bonded fibrous products |
US3309444A (en) | 1962-06-07 | 1967-03-14 | Schueler George Berthol Edward | Method of producing particle board |
US3493527A (en) | 1962-06-07 | 1970-02-03 | George Berthold Edward Schuele | Moldable composition formed of waste wood or the like |
US3516953A (en) | 1968-03-25 | 1970-06-23 | Ernest Herbert Wood | Granular,free-flowing,synthetic thermosetting aminoplast resin molding composition containing defiberized alpha-cellulosic pulp of a certain fiber length wherein said filler is substantially the sole filler present |
US3596314A (en) | 1968-11-26 | 1971-08-03 | Hitco | Apparatus for forming a densified fibrous article |
US3645939A (en) | 1968-02-01 | 1972-02-29 | Us Plywood Champ Papers Inc | Compatibilization of hydroxyl containing materials and thermoplastic polymers |
US3671615A (en) | 1970-11-10 | 1972-06-20 | Reynolds Metals Co | Method of making a composite board product from scrap materials |
US3697364A (en) | 1970-04-16 | 1972-10-10 | Monsanto Co | Discontinuous cellulose reinforced elastomer |
US3709845A (en) | 1971-07-06 | 1973-01-09 | Monsanto Co | Mixed discontinuous fiber reinforced composites |
US3718536A (en) | 1970-04-22 | 1973-02-27 | Thilmany Pulp & Paper Co | Composite board and method of manufacture |
US3836412A (en) | 1970-04-16 | 1974-09-17 | Monsanto Co | Preparation of discontinuous fiber reinforced elastomer |
US3878143A (en) | 1972-11-03 | 1975-04-15 | Sonesson Plast Ab | Method of preventing corrosion in connection with extrusion of mixtures containing polyvinyl chloride and wood flour or similar cellulosic material, and analogous mixtures containing polystyrene or acrylonitrile-butadiene-styrene resin, respectively |
US3888810A (en) | 1972-07-11 | 1975-06-10 | Nippon Oil Co Ltd | Thermoplastic resin composition including wood and fibrous materials |
US3943079A (en) | 1974-03-15 | 1976-03-09 | Monsanto Company | Discontinuous cellulose fiber treated with plastic polymer and lubricant |
US3956555A (en) | 1974-09-23 | 1976-05-11 | Potlatch Corporation | Load carrying member constructed of oriented wood strands and process for making same |
US3956541A (en) | 1974-05-02 | 1976-05-11 | Capital Wire & Cable, Division Of U. S. Industries | Structural member of particulate material and method of making same |
US3985927A (en) | 1975-02-24 | 1976-10-12 | Nekoosa Edwards Paper Company, Inc. | Compositions and method for producing a chemical watermark on finished paper products |
US4005162A (en) | 1974-01-18 | 1977-01-25 | Bison-Werke Bahre & Greten Gmbh & Co. Kg | Process for the continuous production of particle board |
US4016232A (en) | 1974-05-02 | 1977-04-05 | Capital Wire And Cable, Division Of U.S. Industries | Process of making laminated structural member |
US4033913A (en) | 1973-11-19 | 1977-07-05 | Olof Sunden | Cellulose and cellulose products modified by silicic acid |
US4045603A (en) | 1975-10-28 | 1977-08-30 | Nora S. Smith | Construction material of recycled waste thermoplastic synthetic resin and cellulose fibers |
US4056591A (en) | 1973-12-26 | 1977-11-01 | Monsanto Company | Process for controlling orientation of discontinuous fiber in a fiber-reinforced product formed by extrusion |
US4058580A (en) | 1974-12-02 | 1977-11-15 | Flanders Robert D | Process for making a reinforced board from lignocellulosic particles |
GB1503103A (en) | 1975-03-12 | 1978-03-08 | Mitsui Mining & Smelting Co | Method of stripping foreign material from plastics material |
US4097648A (en) | 1975-02-10 | 1978-06-27 | Capital Wire & Cable, Division Of U.S. Industries, Inc. | Laminated structural member and method of making same |
US4112038A (en) | 1976-09-02 | 1978-09-05 | Lowe Paper Company | Method for producing molded articles |
US4113908A (en) | 1972-12-28 | 1978-09-12 | Nippon Oil Company Ltd. | Synthetic paper |
US4115497A (en) | 1975-12-01 | 1978-09-19 | Elopak A/S | Process for the production of pressed bodies from municipal refuse |
US4145389A (en) | 1977-08-22 | 1979-03-20 | Smith Teddy V | Process for making extruded panel product |
US4168251A (en) | 1976-03-13 | 1979-09-18 | Rehau Plastiks Ag & Co. | Plastic-wood powder mixture for making insulating material for the electrical industry |
US4187352A (en) | 1977-04-19 | 1980-02-05 | Lankhorst Touwfabrieken B.V. | Method and apparatus for producing synthetic plastics products, and product produced thereby |
US4204010A (en) | 1976-09-17 | 1980-05-20 | W. R. Grace & Co. | Radiation curable, ethylenically unsaturated thixotropic agent and method of preparation |
US4203876A (en) | 1977-02-28 | 1980-05-20 | Solvay & Cie. | Moldable compositions based on thermoplastic polymers, synthetic elastomers and vegetable fibrous materials, and use of these compositions for calendering and thermoforming |
US4228116A (en) | 1973-03-23 | 1980-10-14 | G.O.R. Applicazioni Speciali S.P.A. | Process for producing remoldable panels |
US4239679A (en) | 1979-06-27 | 1980-12-16 | Diamond Shamrock Corporation | High bulk density rigid poly(vinyl chloride) resin powder composition and preparation thereof |
US4244847A (en) | 1978-08-10 | 1981-01-13 | The Gates Rubber Company | Fibrated admix or polymer and process therefore |
US4244903A (en) | 1976-10-22 | 1981-01-13 | Rolf Schnause | Manufacture of flowable composite particulate material |
US4248743A (en) | 1979-08-17 | 1981-02-03 | Monsanto Company | Preparing a composite of wood pulp dispersed in a polymeric matrix |
US4248820A (en) | 1978-12-21 | 1981-02-03 | Board Of Control Of Michigan Technological University | Method for molding apertures in molded wood products |
US4250222A (en) | 1974-12-31 | 1981-02-10 | Institut National De Recherche Chimique Appliquee | Process for manufacturing finished and semi-finished products from mixtures of various synthetic resin scrap materials |
US4263184A (en) | 1977-01-05 | 1981-04-21 | Wyrough And Loser, Inc. | Homogeneous predispersed fiber compositions |
US4265846A (en) | 1979-10-05 | 1981-05-05 | Canadian Patents And Development Limited | Method of binding lignocellulosic materials |
US4273688A (en) | 1978-09-11 | 1981-06-16 | Desoto, Inc. | Wood textured aqueous latex containing wood particles with sorbed organic solvent |
US4277428A (en) | 1977-09-14 | 1981-07-07 | Masonite Corporation | Post-press molding of man-made boards to produce contoured furniture parts |
US4279790A (en) | 1979-07-05 | 1981-07-21 | Kabushiki Kaisha Mikuni Seisakusho | Composite material compositions using wasterpaper and method of producing same |
US4281039A (en) | 1978-10-06 | 1981-07-28 | Lonseal Corporation | Method for making a vinyl chloride resin sheet and sheet formed by said method |
US4290988A (en) | 1978-10-17 | 1981-09-22 | Casimir Kast Gmbh & Co. Kg | Method for the manufacture of cellulosic fibrous material which can be pressed into moulded parts |
US4303019A (en) | 1979-03-07 | 1981-12-01 | Board Of Control Of Michigan Technological University | Articles molded from papermill sludge |
US4305901A (en) | 1973-07-23 | 1981-12-15 | National Gypsum Company | Wet extrusion of reinforced thermoplastic |
US4311621A (en) | 1979-04-26 | 1982-01-19 | Kikkoman Corporation | Process for producing a filler for adhesive for bonding wood |
US4311554A (en) | 1978-07-19 | 1982-01-19 | Kataflox Patentverwaltungsgesellschaft Mbh. | Incombustible material |
US4318351A (en) | 1978-10-20 | 1982-03-09 | Furnier-U. Sperrholzwerk, J. F. Werz, Jr. Kg, Werzalit-Pressholzwerk | Stackable pallet with integrated stacking members |
US4323625A (en) | 1980-06-13 | 1982-04-06 | Monsanto Company | Composites of grafted olefin polymers and cellulose fibers |
US4328136A (en) | 1980-12-30 | 1982-05-04 | Blount David H | Process for the production of cellulose-silicate products |
US4376144A (en) | 1981-04-08 | 1983-03-08 | Monsanto Company | Treated fibers and bonded composites of cellulose fibers in vinyl chloride polymer characterized by an isocyanate bonding agent |
US4382108A (en) | 1981-12-21 | 1983-05-03 | The Upjohn Company | Novel compositions and process |
US4393020A (en) | 1979-12-20 | 1983-07-12 | The Standard Oil Company | Method for manufacturing a fiber-reinforced thermoplastic molded article |
US4414267A (en) | 1981-04-08 | 1983-11-08 | Monsanto Company | Method for treating discontinuous cellulose fibers characterized by specific polymer to plasticizer and polymer-plasticizer to fiber ratios, fibers thus treated and composites made from the treated fibers |
US4420351A (en) | 1982-04-29 | 1983-12-13 | Tarkett Ab | Method of making decorative laminated products such as tiles, panels or webs from cellulosic materials |
US4426470A (en) | 1981-07-27 | 1984-01-17 | The Dow Chemical Company | Aqueous method of making reinforced composite material from latex, solid polymer and reinforcing material |
US4433813A (en) * | 1979-08-10 | 1984-02-28 | Rodney Whatton | Method for forming wood fibres |
US4440708A (en) | 1978-12-21 | 1984-04-03 | Board Of Control Of Michigan Technological University | Method for molding articles having non-planar portions from matted wood flakes |
US4454091A (en) | 1980-06-10 | 1984-06-12 | Rhone-Poulenc-Textile | Solutions, which can be shaped, from mixtures of cellulose and polyvinyl chloride, and shaped articles resulting therefrom and the process for their manufacture |
US4455709A (en) | 1982-06-16 | 1984-06-26 | Zanini Walter D | Floor mounted guide and shim assembly for sliding doors |
US4458629A (en) | 1980-08-15 | 1984-07-10 | Gerber Milton L | Litter for mammals and fowl |
US4480061A (en) | 1982-12-28 | 1984-10-30 | E. I. Du Pont De Nemours And Company | Wood-like articles made from cellulosic filler loaded ethylene interpolymers |
US4481701A (en) | 1979-08-29 | 1984-11-13 | Hewitt Michael John | Cored plastics profiles and manufacture of frames for windows and the like therefrom |
US4491553A (en) | 1979-07-17 | 1985-01-01 | Lion Corporation | Method for producing filler-loaded thermoplastic resin composite |
US4503115A (en) | 1981-12-04 | 1985-03-05 | Hoechst Aktiengesellschaft | Plate-shaped molded article and process for its preparation and use |
US4505869A (en) | 1982-03-03 | 1985-03-19 | Sadao Nishibori | Method for manufacturing wood-like molded product |
US4506037A (en) | 1983-03-23 | 1985-03-19 | Chuo Kagaku Co., Ltd. | Production of resin foam by aqueous medium |
US4508595A (en) | 1978-05-25 | 1985-04-02 | Stein Gasland | Process for manufacturing of formed products |
US4520530A (en) | 1983-09-02 | 1985-06-04 | Akiva Pinto | Fiber feeding apparatus with a pivoted air exhaust wall portion |
US4551294A (en) | 1983-10-08 | 1985-11-05 | Heochst Aktiengesellschaft | Molding composition based on vinyl chloride polymers, and process for the manufacture of films from these molding compositions for the production of forgery-proof valuable documents |
EP0161766A1 (en) | 1984-03-30 | 1985-11-21 | Kuo Cheng Shen | Composite products from lignocellulosic materials |
US4559376A (en) | 1981-12-11 | 1985-12-17 | Josef Kubat | Method of producing plastic composites filled with cellulose or lignocellulosic materials |
US4562218A (en) | 1982-09-30 | 1985-12-31 | Armstrong World Industries, Inc. | Formable pulp compositions |
US4584357A (en) | 1984-06-20 | 1986-04-22 | Weyerhaeuser Company | Latex treated cationic cellulose product and method for its preparation |
US4594372A (en) | 1983-08-25 | 1986-06-10 | Vish Chimiko-Technologitcheski Institute | Polyvinyl chloride composition |
US4597928A (en) | 1984-03-23 | 1986-07-01 | Leningradsky Tekhnologichesky Institute Tselljulozno-Bumazhnoi Promyshlennosti | Method for fiberboard manufacture |
US4608922A (en) | 1984-05-12 | 1986-09-02 | Poehl Andreas | Frameless high pressure platen press |
US4610900A (en) | 1984-12-19 | 1986-09-09 | Sadao Nishibori | Wood-like molded product of synthetic resin |
GB2171953A (en) | 1985-03-05 | 1986-09-10 | Moeller Hubert | Reinforced profile members and methods of making the same |
US4624890A (en) | 1984-02-15 | 1986-11-25 | Lever Brothers Company | Article suitable for wiping surfaces |
US4632170A (en) | 1984-12-18 | 1986-12-30 | Poehl Andreas | Method and apparatus for making precision metal castings |
US4645631A (en) | 1983-12-22 | 1987-02-24 | Anton Heggenstaller | Process for the extrusion of composite structural members |
US4659754A (en) | 1985-11-18 | 1987-04-21 | Polysar Limited | Dispersions of fibres in rubber |
US4663225A (en) | 1986-05-02 | 1987-05-05 | Allied Corporation | Fiber reinforced composites and method for their manufacture |
US4674414A (en) | 1984-09-20 | 1987-06-23 | Werzaklit-Werke J. F. Werz KG | One-piece pallet with plurality of legs |
US4686251A (en) | 1984-07-27 | 1987-08-11 | Societe Anonyme: Boxy Industries | Method for making decorative resin-wood composites and the resultant product |
US4687793A (en) | 1984-12-25 | 1987-08-18 | Chisso Corporation | Thermoplastic resins containing gloxal heat treated cellulosic fillers |
US4713291A (en) | 1984-09-06 | 1987-12-15 | Mitsubishi Rayon Company Ltd. | Fragrant fiber |
US4716062A (en) | 1985-11-08 | 1987-12-29 | Max Klein | Composite materials, their preparation and articles made therefrom |
US4717742A (en) | 1985-05-29 | 1988-01-05 | Beshay Alphons D | Reinforced polymer composites with wood fibers grafted with silanes - grafting of celluloses or lignocelluloses with silanes to reinforce the polymer composites |
US4717743A (en) | 1985-03-29 | 1988-01-05 | Nippondenso Co., Ltd. | Polyolefin-base resin composition |
US4734236A (en) | 1985-12-02 | 1988-03-29 | Sheller-Globe Corporation | Method for forming fiber web for compression molding structural substrates for panels |
US4737532A (en) | 1984-07-23 | 1988-04-12 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Thermoplastic resin composition containing wood flour |
US4738723A (en) | 1981-12-24 | 1988-04-19 | Gulf States Asphalt Co. | Asbestos-free asphalt composition |
US4746688A (en) | 1987-05-21 | 1988-05-24 | Ford Motor Company | Remoldable, wood-filled acoustic sheet |
US4769274A (en) | 1986-12-22 | 1988-09-06 | Tarkett Inc. | Relatively inexpensive thermoformable mat of reduced density and rigid laminate which incorporates the same |
US4769109A (en) | 1986-12-22 | 1988-09-06 | Tarkett Inc. | Relatively inexpensive thermoformable mat and rigid laminate formed therefrom |
US4791020A (en) | 1987-02-02 | 1988-12-13 | Novacor Chemicals Ltd. | Bonded composites of cellulose fibers polyethylene |
US4810445A (en) | 1986-09-26 | 1989-03-07 | Fortifiber Corporation | Process for making pressboard from poly-coated paper |
US4818604A (en) | 1987-03-27 | 1989-04-04 | Sub-Tank Renewal Systems, Inc. | Composite board and method |
US4833181A (en) | 1986-07-25 | 1989-05-23 | Tonen Sekiyukagaku Kabushiki Kaisha | Polyolefin composition containing cellulose fibers and a deodorizer |
US4851458A (en) | 1986-09-11 | 1989-07-25 | Rehau Ag & Co. | Use of cellulose fibers for structurally modifying polyvinyl chloride articles |
EP0330729A1 (en) | 1988-03-03 | 1989-09-06 | Am International Incorporated | Rotary knife paper trimmer with long life shearing surfaces for trimming thick and shingled paper products |
US4865788A (en) | 1985-12-02 | 1989-09-12 | Sheller-Globe Corporation | Method for forming fiber web for compression molding structural substrates for panels and fiber web |
US4874095A (en) | 1987-06-03 | 1989-10-17 | Signode System Gmbh | Edge protector and method of making same |
US4894192A (en) | 1987-08-05 | 1990-01-16 | Hans Warych | Process for producing molded bodies from paper and a thermoplastic material |
US4911700A (en) | 1985-07-22 | 1990-03-27 | Mcneil-Ppc, Inc. | Cross-linked microfibrillated cellulose prepared from pure generating particles |
US4915764A (en) | 1987-05-23 | 1990-04-10 | Mario Miani | Method of making panels |
US4927579A (en) | 1988-04-08 | 1990-05-22 | The Dow Chemical Company | Method for making fiber-reinforced plastics |
US4929498A (en) | 1989-01-31 | 1990-05-29 | James River Corporation Of Virginia | Engineered-pulp wet wiper fabric |
US4935182A (en) | 1987-02-10 | 1990-06-19 | Menzolit Gmbh | Process for producing a dimensionally stable thermoplastic semifinished product |
AU4781190A (en) | 1989-01-09 | 1990-07-12 | Peter T. Locke | A composite board and method of producing same |
US4944734A (en) | 1989-03-09 | 1990-07-31 | Micro Vesicular Systems, Inc. | Biodegradable incontinence device with embedded granules |
US4960548A (en) | 1986-08-06 | 1990-10-02 | Toyota Jidosha Kabushiki Kaisha | Method of manufacturing molded wooden product |
US4963603A (en) | 1989-05-24 | 1990-10-16 | Armstrong World Industries, Inc. | Composite fiberboard and process of manufacture |
US4968463A (en) | 1987-11-06 | 1990-11-06 | Otvd (Omnium De Traitements Et De Valorisation Des Dechets) | Process for making molded or extruded objects from waste containing plastic materials |
US4973440A (en) | 1989-03-15 | 1990-11-27 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Method for production of fiber-reinforced thermosetting resin molding material |
US4978489A (en) | 1986-07-31 | 1990-12-18 | The Wiggins Teape Group Limited | Process for the manufacture of a permeable sheet-like fibrous structure |
EP0409525A2 (en) | 1989-07-21 | 1991-01-23 | Fortifiber Corporation | Apparatus and method for making pressboard from poly-coated paper using relative movement of facing webs |
US4988478A (en) | 1987-12-16 | 1991-01-29 | Kurt Held | Process for fabricating processed wood material panels |
US5002713A (en) | 1989-12-22 | 1991-03-26 | Board Of Control Of Michigan Technological University | Method for compression molding articles from lignocellulosic materials |
US5008310A (en) | 1989-05-15 | 1991-04-16 | Beshay Alphons D | Polymer composites based cellulose-V |
US5009586A (en) | 1988-12-14 | 1991-04-23 | Pallmann Maschinenfabrik Gmbh & Co. Kg | Agglomerating apparatus for the continuous regranulation of thermoplastic wastes |
US5017319A (en) | 1984-03-30 | 1991-05-21 | Shen Kuo C | Method of making composite products from lignocellulosic materials |
US5028266A (en) | 1987-05-01 | 1991-07-02 | Stephan Rettenmaier | Fiber-filled granules |
US5057167A (en) | 1989-02-02 | 1991-10-15 | Hermann Berstorff Maschinenbau Gmbh | Method for producing chip- and fiber-board webs of uniform thickness |
US5064692A (en) | 1990-02-15 | 1991-11-12 | International Paper Company | Method for producing paper products having increased gloss in which surface characteristics of a release film are imparted to coated substrates |
US5075359A (en) | 1989-10-16 | 1991-12-24 | Ici Americas Inc. | Polymer additive concentrate |
US5075057A (en) | 1991-01-08 | 1991-12-24 | Hoedl Herbert K | Manufacture of molded composite products from scrap plastics |
US5082605A (en) | 1990-03-14 | 1992-01-21 | Advanced Environmental Recycling Technologies, Inc. | Method for making composite material |
US5084135A (en) | 1990-03-27 | 1992-01-28 | Advanced Environmental Recycling Technologies, Inc. | Recycling plastic coated paper product waste |
US5087400A (en) | 1988-01-13 | 1992-02-11 | Wogegal S.A. | Process for making a product serving as a cultivation support |
US5088910A (en) | 1990-03-14 | 1992-02-18 | Advanced Environmental Recycling Technologies, Inc. | System for making synthetic wood products from recycled materials |
US5093058A (en) | 1989-03-20 | 1992-03-03 | Medite Corporation | Apparatus and method of manufacturing synthetic boards |
US5096406A (en) | 1990-03-14 | 1992-03-17 | Advanced Environmental Recycling Technologies, Inc. | Extruder assembly for composite materials |
US5100603A (en) | 1990-04-30 | 1992-03-31 | Neefe Charles W | Method of recycling multimaterial containers |
US5100545A (en) | 1990-12-03 | 1992-03-31 | Advanced Environmental Recycling Technologies, Inc. | Separation tank |
US5102055A (en) | 1990-05-23 | 1992-04-07 | Didier-Werke Ag | Apparatus and process for disintegrating a fiber agglomerate |
US5104411A (en) | 1985-07-22 | 1992-04-14 | Mcneil-Ppc, Inc. | Freeze dried, cross-linked microfibrillated cellulose |
WO1992007995A1 (en) | 1990-10-29 | 1992-05-14 | Tryam Trading Inc. | Treatment of absorbent sanitary paper products |
US5120776A (en) | 1989-04-19 | 1992-06-09 | Govinda Raj | Process for chemical treatment of discontinuous cellulosic fibers and composites of polyethylene and treated fibers |
US5124519A (en) | 1990-01-23 | 1992-06-23 | International Paper Company | Absorbent microwave susceptor composite and related method of manufacture |
US5134023A (en) | 1990-07-05 | 1992-07-28 | Forintek Canada Corp. | Process for making stable fiberboard from used paper and fiberboard made by such process |
US5155147A (en) | 1988-12-08 | 1992-10-13 | Werzalit Aktiengesellschaft & Co. | Method of making a pressible mixture of lignocellulose-containing fibers and a thermoplastic material having stronger bonding between the fibers and the thermoplastic material |
US5164432A (en) | 1989-06-07 | 1992-11-17 | Solvay & Cie | Moulding compositions comprising polyolefins and cellulose fibres, process for their manufacture and objects wrought from these compositions |
US5183837A (en) | 1988-03-30 | 1993-02-02 | Presidenza Del Consiglio Dei Ministri - Ufficio Del Ministro Per Il Coordinamento Delle Iniziativae Per La Ricerca Scientifica E Tecnologica | Process for binding cellulosic materials with a binding agent of an aqueous emulsions of polyisocyanates and cellulose ether |
US5194461A (en) | 1991-06-26 | 1993-03-16 | University Of Northern Iowa Foundation | Structural materials from recycled high density polyethylene and herbaceous fibers, and method for production |
US5213021A (en) | 1990-03-14 | 1993-05-25 | Advanced Environmental Recycling Technologies, Inc. | Reciprocating cutter assembly |
US5234171A (en) * | 1991-05-20 | 1993-08-10 | Cisap S.P.A. | Installation for crushing used vehicle tires and the like, and for separating the metal parts from the non-metal parts of the crushed material |
US5254617A (en) | 1989-11-16 | 1993-10-19 | Mitsui Petrochemical Industries, Ltd. | Resin composition for producing a film and method for producing a film by using the same |
US5268074A (en) | 1990-03-27 | 1993-12-07 | Advanced Environmental Recycling Technologies, Inc. | Method for recycling polymeric film |
US5277758A (en) | 1990-03-27 | 1994-01-11 | Advanced Environmental Recycling Technologies, Inc. | Method for recycling plastic coated paper product waste and polymeric film |
US5284610A (en) | 1993-02-09 | 1994-02-08 | Kang Na Hsiung Enterprise Co., Ltd. | High molecular absorbent sheet manufacturing process and the related equipment |
US5285973A (en) | 1992-07-15 | 1994-02-15 | Advanced Environmental Recycling Technologies, Inc. | Close tolerance shredder |
US5298102A (en) | 1993-01-08 | 1994-03-29 | Sorbilite Inc. | Expanding pressure chamber for bonding skins to flat and shaped articles |
US5331087A (en) | 1990-12-29 | 1994-07-19 | Pwa Industriepapier Gmbh | Method for reprocessing thermoplast-coated packing materials and thermoplast material for further processing |
US5350370A (en) | 1993-04-30 | 1994-09-27 | Kimberly-Clark Corporation | High wicking liquid absorbent composite |
US5366790A (en) | 1991-06-14 | 1994-11-22 | Liebel Henry L | Composite article made from used or surplus corrugated boxes or sheets |
US5372878A (en) | 1992-06-23 | 1994-12-13 | Yamasa Momi Kikaku Co., Ltd. | Slackened or creased fibrous sheet |
US5374474A (en) | 1991-09-26 | 1994-12-20 | Earth Partners, Inc. | Composite board and method of manufacture |
DE4331747A1 (en) | 1993-09-20 | 1995-03-23 | Wuenning Paul | Extruded, fiber-reinforced natural material granulate for thermoplastic processing, and process for its production |
US5406768A (en) | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5416139A (en) | 1993-10-07 | 1995-05-16 | Zeiszler; Dennis E. | Structural building materials or articles obtained from crop plants or residues therefrom and/or polyolefin materials |
US5421205A (en) | 1992-02-14 | 1995-06-06 | Carl Schenck Ag | Apparatus for the rapid ultimate material strength testing of test samples |
US5432000A (en) | 1989-03-20 | 1995-07-11 | Weyerhaeuser Company | Binder coated discontinuous fibers with adhered particulate materials |
US5437766A (en) | 1993-10-22 | 1995-08-01 | The Procter & Gamble Company | Multi-ply facial tissue paper product comprising biodegradable chemical softening compositions and binder materials |
US5439749A (en) | 1994-08-18 | 1995-08-08 | Andersen Corporation | Composite wood structure |
US5441801A (en) | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5480602A (en) | 1994-06-17 | 1996-01-02 | Nagaich; Laxmi | Extruded particle board |
US5486553A (en) | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5498478A (en) | 1989-03-20 | 1996-03-12 | Weyerhaeuser Company | Polyethylene glycol as a binder material for fibers |
US5516585A (en) | 1989-03-20 | 1996-05-14 | Weyerhaeuser Company | Coated fiber product with adhered super absorbent particles |
US5516472A (en) | 1993-11-12 | 1996-05-14 | Strandex Corporation | Extruded synthetic wood composition and method for making same |
US5540244A (en) | 1993-12-07 | 1996-07-30 | Advanced Environmental Recycling Technologies, Inc. | Method and apparatus for cleaning and recycling post-consumer plastic films |
US5543205A (en) | 1991-06-14 | 1996-08-06 | Corrcycle, Inc. | Composite article made from used or surplus corrugated boxes or sheets |
US5547745A (en) | 1992-08-17 | 1996-08-20 | Weyerhaeuser Company | Particle binders |
US5558933A (en) | 1989-07-24 | 1996-09-24 | Aci International Limited | Sheeting material and method of manufacturing the same |
US5571618A (en) | 1992-08-17 | 1996-11-05 | Weyerhaeuser Company | Reactivatable binders for binding particles to fibers |
US5574094A (en) | 1991-10-31 | 1996-11-12 | Montell North America Inc. | Polyolefin compositions and process for their preparation |
US5582847A (en) | 1993-05-28 | 1996-12-10 | Repete Corporation | Optimizing pellet mill controller |
US5582682A (en) | 1988-12-28 | 1996-12-10 | Ferretti; Arthur | Process and a composition for making cellulosic composites |
US5585150A (en) | 1994-09-08 | 1996-12-17 | Mulch Developement Company | Mulch product and process for its preparation |
US5585155A (en) | 1995-06-07 | 1996-12-17 | Andersen Corporation | Fiber reinforced thermoplastic structural member |
US5614570A (en) | 1992-08-17 | 1997-03-25 | Weyerhaeuser Company | Absorbent articles containing binder carrying high bulk fibers |
US5618858A (en) | 1993-07-05 | 1997-04-08 | Siemens Aktiengesellschaft | Polymer material |
US5643635A (en) | 1994-02-16 | 1997-07-01 | Chan-Hee Shin | Method and composition for forming a decorative coating on a substrate |
US5643359A (en) | 1995-11-15 | 1997-07-01 | Dpd, Inc. | Dispersion of plant pulp in concrete and use thereof |
US5663216A (en) | 1993-07-28 | 1997-09-02 | Bio-Tec Biologische Naturverpackungen Gmbh | Reinforced biodegradable polymer |
EP0801168A1 (en) | 1996-04-09 | 1997-10-15 | Ein Engineering Co., Ltd. | Method and apparatus for recycling laminated film |
US5682015A (en) | 1993-10-15 | 1997-10-28 | Georgia Power Company | Squirrel shield device |
US5746958A (en) | 1995-03-30 | 1998-05-05 | Trex Company, L.L.C. | Method of producing a wood-thermoplastic composite material |
US5759680A (en) | 1990-03-14 | 1998-06-02 | Advanced Environmetal Recycling Technologies, Inc. | Extruded composite profile |
US5767177A (en) | 1993-05-04 | 1998-06-16 | Cytec Industry Incorporated | Injection mouldable thermosetting composition especially for motor vehicle bodies, method of production and method or recycling |
US5773138A (en) | 1992-08-31 | 1998-06-30 | Andersen Corporation | Advanced compatible polymer wood fiber composite |
US5791262A (en) | 1994-02-14 | 1998-08-11 | The Fabri-Form Co. | Reinforced plastic pallet |
US5819491A (en) | 1996-01-22 | 1998-10-13 | L.B. Plastics Limited | Modular construction elements |
US5824246A (en) | 1991-03-29 | 1998-10-20 | Engineered Composites | Method of forming a thermoactive binder composite |
US5827607A (en) | 1992-08-31 | 1998-10-27 | Andersen Corporation | Advanced polymer wood composite |
US5851469A (en) | 1995-12-27 | 1998-12-22 | Trex Company, L.L.C. | Process for making a wood-thermoplastic composite |
US5871162A (en) * | 1998-01-02 | 1999-02-16 | Robert C. Rajewski | Paper shredding assembly |
US5876641A (en) | 1995-07-31 | 1999-03-02 | Andersen Corporation | In-line process for injection of foam material into a composite profile |
US5882564A (en) | 1996-06-24 | 1999-03-16 | Andersen Corporation | Resin and wood fiber composite profile extrusion method |
US5948505A (en) | 1997-03-28 | 1999-09-07 | Andersen Corporation | Thermoplastic resin and fiberglass fabric composite and method |
US5948524A (en) | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US5952105A (en) | 1997-09-02 | 1999-09-14 | Xyleco, Inc. | Poly-coated paper composites |
US5973035A (en) | 1997-10-31 | 1999-10-26 | Xyleco, Inc. | Cellulosic fiber composites |
US5981067A (en) | 1992-08-31 | 1999-11-09 | Andersen Corporation | Advanced compatible polymer wood fiber composite |
US5985429A (en) | 1992-08-31 | 1999-11-16 | Andersen Corporation | Polymer fiber composite with mechanical properties enhanced by particle size distribution |
US6004668A (en) | 1992-08-31 | 1999-12-21 | Andersen Corporation | Advanced polymer wood composite |
US6029916A (en) * | 1998-01-16 | 2000-02-29 | Terra Technologies, Inc. | System and method for decomposing reclaiming and refusing waste carpet materials |
US6054207A (en) | 1998-01-21 | 2000-04-25 | Andersen Corporation | Foamed thermoplastic polymer and wood fiber profile and member |
US6085923A (en) | 1996-08-13 | 2000-07-11 | Neocork Technologies, Inc. | Composite synthetic stopper |
US6117924A (en) | 1996-10-22 | 2000-09-12 | Crane Plastics Company Limited Partnership | Extrusion of synthetic wood material |
US6122877A (en) | 1997-05-30 | 2000-09-26 | Andersen Corporation | Fiber-polymeric composite siding unit and method of manufacture |
WO2000078127A1 (en) | 1999-06-22 | 2000-12-28 | Xyleco, Inc. | Texturized cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6180257B1 (en) | 1996-10-29 | 2001-01-30 | Crane Plastics Company Limited Partnership | Compression molding of synthetic wood material |
US6200682B1 (en) | 1996-12-11 | 2001-03-13 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials and products made by the method |
US6265037B1 (en) | 1999-04-16 | 2001-07-24 | Andersen Corporation | Polyolefin wood fiber composite |
US6270883B1 (en) | 1998-10-09 | 2001-08-07 | The United States Of America As Represented By The Secretary Of Agriculture | Composites containing cellulosic pulp fibers and methods of making and using the same |
US6284098B1 (en) | 1998-07-20 | 2001-09-04 | Wwj, Llc | Lignocellulose fiber filler for thermoplastic composite compositions |
US6322664B1 (en) * | 2000-10-17 | 2001-11-27 | Voith Sulzer Paper Technology North America, Inc. | Method of processing recycled waste paper by separating fibers of different colors |
US6337138B1 (en) | 1998-12-28 | 2002-01-08 | Crane Plastics Company Limited Partnership | Cellulosic, inorganic-filled plastic composite |
US20020010229A1 (en) | 1997-09-02 | 2002-01-24 | Marshall Medoff | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6344268B1 (en) | 1998-04-03 | 2002-02-05 | Certainteed Corporation | Foamed polymer-fiber composite |
US20020019614A1 (en) | 2000-05-17 | 2002-02-14 | Woon Paul S. | Absorbent articles having improved performance |
WO2002014039A1 (en) | 2000-08-10 | 2002-02-21 | California Agriboard, Llc. | Production of particle board from agricultural waste |
US6357197B1 (en) | 1997-02-05 | 2002-03-19 | Andersen Corporation | Polymer covered advanced polymer/wood composite structural member |
US6409952B1 (en) | 1998-11-25 | 2002-06-25 | Crane Plastics Company Limited Partnership | Drying and processing cellulosic compounds |
US6420626B1 (en) | 1999-06-08 | 2002-07-16 | Buckeye Technologies Inc. | Unitary fluid acquisition, storage, and wicking material |
US6425979B1 (en) | 1992-08-17 | 2002-07-30 | Weyerhaeuser Company | Method for making superabsorbent containing diapers |
US6448307B1 (en) | 1997-09-02 | 2002-09-10 | Xyleco, Inc. | Compositions of texturized fibrous materials |
US6479002B1 (en) | 1998-12-30 | 2002-11-12 | Haller Formholz | Extrusion of plant materials encapsulated in a thermoplastic |
US6495225B1 (en) | 1998-12-25 | 2002-12-17 | Konica Corporation | Molding material |
US20030021915A1 (en) | 2001-06-15 | 2003-01-30 | Vivek Rohatgi | Cellulose - polymer composites and related manufacturing methods |
US20030032702A1 (en) | 1997-09-02 | 2003-02-13 | Marshall Medoff | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US20030100634A1 (en) | 2001-04-16 | 2003-05-29 | Heath Richard B. | Composite compositions |
US20030121380A1 (en) | 2001-11-30 | 2003-07-03 | Cowell Christine M. | System for aperturing and coaperturing webs and web assemblies |
US20030125688A1 (en) | 2001-11-30 | 2003-07-03 | Keane James M. | Adhesive system for mechanically post-treated absorbent structures |
US6605245B1 (en) | 1997-12-11 | 2003-08-12 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials |
US6617376B2 (en) | 2001-03-30 | 2003-09-09 | Crane Plastics Company Llc | Flexible wood composition |
US6620503B2 (en) | 2000-07-26 | 2003-09-16 | Kimberly-Clark Worldwide, Inc. | Synthetic fiber nonwoven web and method |
US20030187102A1 (en) | 1997-09-02 | 2003-10-02 | Marshall Medoff | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US6632863B2 (en) | 2001-10-25 | 2003-10-14 | Crane Plastics Company Llc | Cellulose/polyolefin composite pellet |
US6638612B2 (en) | 2000-09-18 | 2003-10-28 | James D. Jones | Thermoplastic composite wood material |
US20030207064A1 (en) | 1996-04-29 | 2003-11-06 | Bunyan Michael H. | Conformal thermal interface material for electronic components |
US6670035B2 (en) | 2002-04-05 | 2003-12-30 | Arteva North America S.A.R.L. | Binder fiber and nonwoven web |
US20040005461A1 (en) | 1996-07-11 | 2004-01-08 | Nagle Dennis C. | Carbonized wood-based materials |
US6685858B2 (en) | 1997-09-05 | 2004-02-03 | Crane Plastics Company Llc | In-line compounding and extrusion system |
US20040072924A1 (en) | 2002-10-09 | 2004-04-15 | Crompton Corporation | Natural fiber-filled polyolefin composites |
US6743507B2 (en) | 2002-06-07 | 2004-06-01 | Rayonier Products And Financial Services Company | Cellulose fiber reinforced composites having reduced discoloration and improved dispersion and associated methods of manufacture |
US6746976B1 (en) | 1999-09-24 | 2004-06-08 | The Procter & Gamble Company | Thin until wet structures for acquiring aqueous fluids |
US6758996B2 (en) | 2001-07-13 | 2004-07-06 | Kadant Composites Inc. | Cellulose-reinforced thermoplastic composite and methods of making same |
US20040140069A1 (en) * | 2001-04-23 | 2004-07-22 | Roland Selin | Production of fiber suspension from waste paper |
US6780359B1 (en) | 2002-01-29 | 2004-08-24 | Crane Plastics Company Llc | Synthetic wood composite material and method for molding |
US6784230B1 (en) | 1999-09-23 | 2004-08-31 | Rohm And Haas Company | Chlorinated vinyl resin/cellulosic blends: compositions, processes, composites, and articles therefrom |
US6821614B1 (en) | 1996-12-11 | 2004-11-23 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials, and products made by the method |
US6855182B2 (en) | 2002-07-17 | 2005-02-15 | Rayonier Products And Financial Services Company | Lignocellulose fiber composite with soil conditioners |
US6969781B2 (en) | 1997-05-13 | 2005-11-29 | Weyeerhaeuser Company | Reticulated absorbent composite |
US20060247336A1 (en) | 1999-06-22 | 2006-11-02 | Xyleco, Inc., A Massachusetts Corporation | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US7708214B2 (en) * | 2005-08-24 | 2010-05-04 | Xyleco, Inc. | Fibrous materials and composites |
Family Cites Families (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US587162A (en) * | 1897-07-27 | Frank rosebrook | ||
US1057101A (en) * | 1908-04-29 | 1913-03-25 | Louis E F Wachter | Watch screw-driver. |
AU3566371A (en) * | 1970-11-27 | 1973-05-17 | Radiation Dev Co Ltd | Method and apparatus for treating wood chips |
AT338499B (en) * | 1973-09-12 | 1977-08-25 | Oesterr Studien Atomenergie | Process for the production of plastic-impregnated wood chipboard or wood fiber hardboard |
US4053112A (en) * | 1973-12-13 | 1977-10-11 | The Andersons | Corn cob processing apparatus and method |
US4236897A (en) * | 1978-09-18 | 1980-12-02 | Johnston Ian F | Fuel pellets |
WO1980000142A1 (en) * | 1978-07-06 | 1980-02-07 | A Akesson | A method of manufacturing bonded products of cellulose or cellulose derivatives |
US4246295A (en) * | 1978-09-15 | 1981-01-20 | Crihan Ioan G | Sterilization and structural reinforcement of art objects made of organic material |
SU1102929A1 (en) * | 1982-12-29 | 1984-07-15 | Донецкий Филиал Научно-Исследовательского Горнорудного Института | Pneumatic percussion mechanism |
AU8101491A (en) * | 1990-06-29 | 1992-01-23 | Gui Gerard De Jager | A process for manufacturing reinforced composites and filament material for use in said process |
SE502387C2 (en) * | 1993-06-23 | 1995-10-09 | Stora Kopparbergs Bergslags Ab | Vibrated cellulose product, methods of preparation thereof and absorbent body |
DE19738953C1 (en) * | 1997-09-05 | 1999-03-04 | Fritz Egger Ges M B H & Co | Method and device for the production of molded articles from comminuted material |
ATE307704T1 (en) * | 1998-09-09 | 2005-11-15 | Para Chemie Gmbh | METHOD FOR PRODUCING WOOD-PLASTIC COMBINATIONS USING HIGH-PERFORMANCE ELECTRON ACCELERATORS |
US6521152B1 (en) * | 2000-03-16 | 2003-02-18 | Honeywell International Inc. | Method for forming fiber reinforced composite parts |
US6309454B1 (en) * | 2000-05-12 | 2001-10-30 | Johnson & Johnson Medical Limited | Freeze-dried composite materials and processes for the production thereof |
US6737464B1 (en) | 2000-05-30 | 2004-05-18 | University Of South Carolina Research Foundation | Polymer nanocomposite comprising a matrix polymer and a layered clay material having a low quartz content |
CA2439632A1 (en) | 2001-03-02 | 2002-09-12 | Southern Clay Products, Inc. | Preparation of polymer nanocomposites by dispersion destabilization |
WO2003018642A1 (en) * | 2001-08-23 | 2003-03-06 | John Lyndon Garnett | Preparation of polymer composites |
WO2003035740A1 (en) * | 2001-10-24 | 2003-05-01 | Temple-Inland Forest Products Corporation | Saccharide-based resin for the preparation of composite products |
US20030186052A1 (en) * | 2002-03-29 | 2003-10-02 | Cytech Fiber Processing Systems, Inc. | Fiber pellets and processes for forming fiber pellets |
RU2217533C1 (en) * | 2002-12-06 | 2003-11-27 | Открытое акционерное общество "Научно-исследовательский институт нетканых материалов" | Nonwoven material and method for manufacture of non-woven material |
US20050000669A1 (en) * | 2003-03-14 | 2005-01-06 | Hugh West | Saccharide treated cellulose pulp sheets |
EP2564931B1 (en) * | 2005-03-24 | 2014-08-06 | Xyleco, Inc. | Methods of making fibrous materials |
-
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Patent Citations (311)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1057151A (en) * | 1911-08-31 | 1913-03-25 | Guy C Howard | Process for the production of mechanical wood-pulp. |
US1405944A (en) * | 1919-04-23 | 1922-02-07 | Shartle Continuous Beater Comp | Process of manufacturing paper pulp |
US1824221A (en) | 1928-10-24 | 1931-09-22 | Masonite Corp | Process and apparatus for disintegration of fibrous material |
US1897620A (en) * | 1932-01-15 | 1933-02-14 | Respats Inc | Continuous process of reducing or reforming wood or other fibrous material |
US2519442A (en) | 1944-04-28 | 1950-08-22 | Saint Gobain | Compositions containing cellulosic filler united by polyvinyl chloride |
US2516847A (en) | 1944-12-01 | 1950-08-01 | Masonite Corp | Process of sizing exploded fibers |
US2558378A (en) | 1947-01-15 | 1951-06-26 | Delaware Floor Products Inc | Composition for floor and wall covering comprising plasticized vinyl resin and filler and method of making same |
US2635976A (en) | 1948-06-15 | 1953-04-21 | Plywood Res Foundation | Method of making synthetic constructional boards and products thereof |
US2658828A (en) | 1948-09-15 | 1953-11-10 | Chemloch Corp | Process of combining synthetic resins and other materials with cellulose |
US2665261A (en) | 1950-05-12 | 1954-01-05 | Allied Chem & Dye Corp | Production of articles of high impact strength |
US2680102A (en) | 1952-07-03 | 1954-06-01 | Homasote Company | Fire-resistant product from comminuted woody material, urea, or melamine-formaldehyde, chlorinated hydrocarbon resin, and hydrated alumina |
US2757150A (en) | 1953-01-30 | 1956-07-31 | Weyerhaeuser Timber Co | Preparing hot-moldable thermosetting resin and cellulose fiber mixtures |
US2877953A (en) * | 1953-09-29 | 1959-03-17 | Weyerhaeuser Timber Co | Granular sclerenchyma and the method of its production from douglas fir bark |
US2935763A (en) | 1954-09-01 | 1960-05-10 | Us Rubber Co | Method of forming pellets of a synthetic rubber latex and a particulate resin |
US2789903A (en) | 1954-09-02 | 1957-04-23 | Celanese Corp | Process for production of shaped articles comprising fibrous particles and a copolymer of vinyl acetate and an ethylenically unsaturated acid |
US3308218A (en) | 1961-05-24 | 1967-03-07 | Wood Conversion Co | Method for producing bonded fibrous products |
US3309444A (en) | 1962-06-07 | 1967-03-14 | Schueler George Berthol Edward | Method of producing particle board |
US3493527A (en) | 1962-06-07 | 1970-02-03 | George Berthold Edward Schuele | Moldable composition formed of waste wood or the like |
US3645939A (en) | 1968-02-01 | 1972-02-29 | Us Plywood Champ Papers Inc | Compatibilization of hydroxyl containing materials and thermoplastic polymers |
US3516953A (en) | 1968-03-25 | 1970-06-23 | Ernest Herbert Wood | Granular,free-flowing,synthetic thermosetting aminoplast resin molding composition containing defiberized alpha-cellulosic pulp of a certain fiber length wherein said filler is substantially the sole filler present |
US3596314A (en) | 1968-11-26 | 1971-08-03 | Hitco | Apparatus for forming a densified fibrous article |
US3836412A (en) | 1970-04-16 | 1974-09-17 | Monsanto Co | Preparation of discontinuous fiber reinforced elastomer |
US3697364A (en) | 1970-04-16 | 1972-10-10 | Monsanto Co | Discontinuous cellulose reinforced elastomer |
US3718536A (en) | 1970-04-22 | 1973-02-27 | Thilmany Pulp & Paper Co | Composite board and method of manufacture |
US3671615A (en) | 1970-11-10 | 1972-06-20 | Reynolds Metals Co | Method of making a composite board product from scrap materials |
US3709845A (en) | 1971-07-06 | 1973-01-09 | Monsanto Co | Mixed discontinuous fiber reinforced composites |
US3888810A (en) | 1972-07-11 | 1975-06-10 | Nippon Oil Co Ltd | Thermoplastic resin composition including wood and fibrous materials |
US3878143A (en) | 1972-11-03 | 1975-04-15 | Sonesson Plast Ab | Method of preventing corrosion in connection with extrusion of mixtures containing polyvinyl chloride and wood flour or similar cellulosic material, and analogous mixtures containing polystyrene or acrylonitrile-butadiene-styrene resin, respectively |
US4113908A (en) | 1972-12-28 | 1978-09-12 | Nippon Oil Company Ltd. | Synthetic paper |
US4228116A (en) | 1973-03-23 | 1980-10-14 | G.O.R. Applicazioni Speciali S.P.A. | Process for producing remoldable panels |
US4305901A (en) | 1973-07-23 | 1981-12-15 | National Gypsum Company | Wet extrusion of reinforced thermoplastic |
US4033913A (en) | 1973-11-19 | 1977-07-05 | Olof Sunden | Cellulose and cellulose products modified by silicic acid |
US4056591A (en) | 1973-12-26 | 1977-11-01 | Monsanto Company | Process for controlling orientation of discontinuous fiber in a fiber-reinforced product formed by extrusion |
US4005162A (en) | 1974-01-18 | 1977-01-25 | Bison-Werke Bahre & Greten Gmbh & Co. Kg | Process for the continuous production of particle board |
US3943079A (en) | 1974-03-15 | 1976-03-09 | Monsanto Company | Discontinuous cellulose fiber treated with plastic polymer and lubricant |
US3956541A (en) | 1974-05-02 | 1976-05-11 | Capital Wire & Cable, Division Of U. S. Industries | Structural member of particulate material and method of making same |
US4016232A (en) | 1974-05-02 | 1977-04-05 | Capital Wire And Cable, Division Of U.S. Industries | Process of making laminated structural member |
US3956555A (en) | 1974-09-23 | 1976-05-11 | Potlatch Corporation | Load carrying member constructed of oriented wood strands and process for making same |
US4058580A (en) | 1974-12-02 | 1977-11-15 | Flanders Robert D | Process for making a reinforced board from lignocellulosic particles |
US4250222A (en) | 1974-12-31 | 1981-02-10 | Institut National De Recherche Chimique Appliquee | Process for manufacturing finished and semi-finished products from mixtures of various synthetic resin scrap materials |
US4097648A (en) | 1975-02-10 | 1978-06-27 | Capital Wire & Cable, Division Of U.S. Industries, Inc. | Laminated structural member and method of making same |
US3985927A (en) | 1975-02-24 | 1976-10-12 | Nekoosa Edwards Paper Company, Inc. | Compositions and method for producing a chemical watermark on finished paper products |
GB1503103A (en) | 1975-03-12 | 1978-03-08 | Mitsui Mining & Smelting Co | Method of stripping foreign material from plastics material |
US4045603A (en) | 1975-10-28 | 1977-08-30 | Nora S. Smith | Construction material of recycled waste thermoplastic synthetic resin and cellulose fibers |
US4115497A (en) | 1975-12-01 | 1978-09-19 | Elopak A/S | Process for the production of pressed bodies from municipal refuse |
US4168251A (en) | 1976-03-13 | 1979-09-18 | Rehau Plastiks Ag & Co. | Plastic-wood powder mixture for making insulating material for the electrical industry |
US4112038A (en) | 1976-09-02 | 1978-09-05 | Lowe Paper Company | Method for producing molded articles |
US4204010A (en) | 1976-09-17 | 1980-05-20 | W. R. Grace & Co. | Radiation curable, ethylenically unsaturated thixotropic agent and method of preparation |
US4244903A (en) | 1976-10-22 | 1981-01-13 | Rolf Schnause | Manufacture of flowable composite particulate material |
US4263184A (en) | 1977-01-05 | 1981-04-21 | Wyrough And Loser, Inc. | Homogeneous predispersed fiber compositions |
US4203876A (en) | 1977-02-28 | 1980-05-20 | Solvay & Cie. | Moldable compositions based on thermoplastic polymers, synthetic elastomers and vegetable fibrous materials, and use of these compositions for calendering and thermoforming |
US4187352A (en) | 1977-04-19 | 1980-02-05 | Lankhorst Touwfabrieken B.V. | Method and apparatus for producing synthetic plastics products, and product produced thereby |
US4145389A (en) | 1977-08-22 | 1979-03-20 | Smith Teddy V | Process for making extruded panel product |
US4277428A (en) | 1977-09-14 | 1981-07-07 | Masonite Corporation | Post-press molding of man-made boards to produce contoured furniture parts |
US4508595A (en) | 1978-05-25 | 1985-04-02 | Stein Gasland | Process for manufacturing of formed products |
US4311554A (en) | 1978-07-19 | 1982-01-19 | Kataflox Patentverwaltungsgesellschaft Mbh. | Incombustible material |
US4244847A (en) | 1978-08-10 | 1981-01-13 | The Gates Rubber Company | Fibrated admix or polymer and process therefore |
US4273688A (en) | 1978-09-11 | 1981-06-16 | Desoto, Inc. | Wood textured aqueous latex containing wood particles with sorbed organic solvent |
US4281039A (en) | 1978-10-06 | 1981-07-28 | Lonseal Corporation | Method for making a vinyl chloride resin sheet and sheet formed by said method |
US4290988A (en) | 1978-10-17 | 1981-09-22 | Casimir Kast Gmbh & Co. Kg | Method for the manufacture of cellulosic fibrous material which can be pressed into moulded parts |
US4318351A (en) | 1978-10-20 | 1982-03-09 | Furnier-U. Sperrholzwerk, J. F. Werz, Jr. Kg, Werzalit-Pressholzwerk | Stackable pallet with integrated stacking members |
US4248820A (en) | 1978-12-21 | 1981-02-03 | Board Of Control Of Michigan Technological University | Method for molding apertures in molded wood products |
US4440708A (en) | 1978-12-21 | 1984-04-03 | Board Of Control Of Michigan Technological University | Method for molding articles having non-planar portions from matted wood flakes |
US4303019A (en) | 1979-03-07 | 1981-12-01 | Board Of Control Of Michigan Technological University | Articles molded from papermill sludge |
US4311621A (en) | 1979-04-26 | 1982-01-19 | Kikkoman Corporation | Process for producing a filler for adhesive for bonding wood |
US4239679A (en) | 1979-06-27 | 1980-12-16 | Diamond Shamrock Corporation | High bulk density rigid poly(vinyl chloride) resin powder composition and preparation thereof |
US4279790A (en) | 1979-07-05 | 1981-07-21 | Kabushiki Kaisha Mikuni Seisakusho | Composite material compositions using wasterpaper and method of producing same |
US4491553A (en) | 1979-07-17 | 1985-01-01 | Lion Corporation | Method for producing filler-loaded thermoplastic resin composite |
US4433813A (en) * | 1979-08-10 | 1984-02-28 | Rodney Whatton | Method for forming wood fibres |
US4248743A (en) | 1979-08-17 | 1981-02-03 | Monsanto Company | Preparing a composite of wood pulp dispersed in a polymeric matrix |
US4481701A (en) | 1979-08-29 | 1984-11-13 | Hewitt Michael John | Cored plastics profiles and manufacture of frames for windows and the like therefrom |
US4265846A (en) | 1979-10-05 | 1981-05-05 | Canadian Patents And Development Limited | Method of binding lignocellulosic materials |
US4393020A (en) | 1979-12-20 | 1983-07-12 | The Standard Oil Company | Method for manufacturing a fiber-reinforced thermoplastic molded article |
US4454091A (en) | 1980-06-10 | 1984-06-12 | Rhone-Poulenc-Textile | Solutions, which can be shaped, from mixtures of cellulose and polyvinyl chloride, and shaped articles resulting therefrom and the process for their manufacture |
US4323625A (en) | 1980-06-13 | 1982-04-06 | Monsanto Company | Composites of grafted olefin polymers and cellulose fibers |
US4458629A (en) | 1980-08-15 | 1984-07-10 | Gerber Milton L | Litter for mammals and fowl |
US4328136A (en) | 1980-12-30 | 1982-05-04 | Blount David H | Process for the production of cellulose-silicate products |
US4414267A (en) | 1981-04-08 | 1983-11-08 | Monsanto Company | Method for treating discontinuous cellulose fibers characterized by specific polymer to plasticizer and polymer-plasticizer to fiber ratios, fibers thus treated and composites made from the treated fibers |
US4376144A (en) | 1981-04-08 | 1983-03-08 | Monsanto Company | Treated fibers and bonded composites of cellulose fibers in vinyl chloride polymer characterized by an isocyanate bonding agent |
US4426470A (en) | 1981-07-27 | 1984-01-17 | The Dow Chemical Company | Aqueous method of making reinforced composite material from latex, solid polymer and reinforcing material |
US4503115A (en) | 1981-12-04 | 1985-03-05 | Hoechst Aktiengesellschaft | Plate-shaped molded article and process for its preparation and use |
US4559376A (en) | 1981-12-11 | 1985-12-17 | Josef Kubat | Method of producing plastic composites filled with cellulose or lignocellulosic materials |
US4382108A (en) | 1981-12-21 | 1983-05-03 | The Upjohn Company | Novel compositions and process |
US4738723A (en) | 1981-12-24 | 1988-04-19 | Gulf States Asphalt Co. | Asbestos-free asphalt composition |
US4505869A (en) | 1982-03-03 | 1985-03-19 | Sadao Nishibori | Method for manufacturing wood-like molded product |
US4420351A (en) | 1982-04-29 | 1983-12-13 | Tarkett Ab | Method of making decorative laminated products such as tiles, panels or webs from cellulosic materials |
US4455709A (en) | 1982-06-16 | 1984-06-26 | Zanini Walter D | Floor mounted guide and shim assembly for sliding doors |
US4562218A (en) | 1982-09-30 | 1985-12-31 | Armstrong World Industries, Inc. | Formable pulp compositions |
US4480061A (en) | 1982-12-28 | 1984-10-30 | E. I. Du Pont De Nemours And Company | Wood-like articles made from cellulosic filler loaded ethylene interpolymers |
US4506037A (en) | 1983-03-23 | 1985-03-19 | Chuo Kagaku Co., Ltd. | Production of resin foam by aqueous medium |
US4594372A (en) | 1983-08-25 | 1986-06-10 | Vish Chimiko-Technologitcheski Institute | Polyvinyl chloride composition |
US4520530A (en) | 1983-09-02 | 1985-06-04 | Akiva Pinto | Fiber feeding apparatus with a pivoted air exhaust wall portion |
US4551294A (en) | 1983-10-08 | 1985-11-05 | Heochst Aktiengesellschaft | Molding composition based on vinyl chloride polymers, and process for the manufacture of films from these molding compositions for the production of forgery-proof valuable documents |
US4645631A (en) | 1983-12-22 | 1987-02-24 | Anton Heggenstaller | Process for the extrusion of composite structural members |
US4624890A (en) | 1984-02-15 | 1986-11-25 | Lever Brothers Company | Article suitable for wiping surfaces |
US4597928A (en) | 1984-03-23 | 1986-07-01 | Leningradsky Tekhnologichesky Institute Tselljulozno-Bumazhnoi Promyshlennosti | Method for fiberboard manufacture |
EP0161766A1 (en) | 1984-03-30 | 1985-11-21 | Kuo Cheng Shen | Composite products from lignocellulosic materials |
US5017319A (en) | 1984-03-30 | 1991-05-21 | Shen Kuo C | Method of making composite products from lignocellulosic materials |
US4608922A (en) | 1984-05-12 | 1986-09-02 | Poehl Andreas | Frameless high pressure platen press |
US4584357A (en) | 1984-06-20 | 1986-04-22 | Weyerhaeuser Company | Latex treated cationic cellulose product and method for its preparation |
US4737532A (en) | 1984-07-23 | 1988-04-12 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Thermoplastic resin composition containing wood flour |
US4686251A (en) | 1984-07-27 | 1987-08-11 | Societe Anonyme: Boxy Industries | Method for making decorative resin-wood composites and the resultant product |
US4713291A (en) | 1984-09-06 | 1987-12-15 | Mitsubishi Rayon Company Ltd. | Fragrant fiber |
US4674414A (en) | 1984-09-20 | 1987-06-23 | Werzaklit-Werke J. F. Werz KG | One-piece pallet with plurality of legs |
US4632170A (en) | 1984-12-18 | 1986-12-30 | Poehl Andreas | Method and apparatus for making precision metal castings |
US4610900A (en) | 1984-12-19 | 1986-09-09 | Sadao Nishibori | Wood-like molded product of synthetic resin |
US4687793A (en) | 1984-12-25 | 1987-08-18 | Chisso Corporation | Thermoplastic resins containing gloxal heat treated cellulosic fillers |
GB2171953A (en) | 1985-03-05 | 1986-09-10 | Moeller Hubert | Reinforced profile members and methods of making the same |
US4717743A (en) | 1985-03-29 | 1988-01-05 | Nippondenso Co., Ltd. | Polyolefin-base resin composition |
US4717742A (en) | 1985-05-29 | 1988-01-05 | Beshay Alphons D | Reinforced polymer composites with wood fibers grafted with silanes - grafting of celluloses or lignocelluloses with silanes to reinforce the polymer composites |
US4911700A (en) | 1985-07-22 | 1990-03-27 | Mcneil-Ppc, Inc. | Cross-linked microfibrillated cellulose prepared from pure generating particles |
US5104411A (en) | 1985-07-22 | 1992-04-14 | Mcneil-Ppc, Inc. | Freeze dried, cross-linked microfibrillated cellulose |
US4716062A (en) | 1985-11-08 | 1987-12-29 | Max Klein | Composite materials, their preparation and articles made therefrom |
US4659754A (en) | 1985-11-18 | 1987-04-21 | Polysar Limited | Dispersions of fibres in rubber |
US4734236A (en) | 1985-12-02 | 1988-03-29 | Sheller-Globe Corporation | Method for forming fiber web for compression molding structural substrates for panels |
US4865788A (en) | 1985-12-02 | 1989-09-12 | Sheller-Globe Corporation | Method for forming fiber web for compression molding structural substrates for panels and fiber web |
US4663225A (en) | 1986-05-02 | 1987-05-05 | Allied Corporation | Fiber reinforced composites and method for their manufacture |
US4833181A (en) | 1986-07-25 | 1989-05-23 | Tonen Sekiyukagaku Kabushiki Kaisha | Polyolefin composition containing cellulose fibers and a deodorizer |
US4978489A (en) | 1986-07-31 | 1990-12-18 | The Wiggins Teape Group Limited | Process for the manufacture of a permeable sheet-like fibrous structure |
US4960548A (en) | 1986-08-06 | 1990-10-02 | Toyota Jidosha Kabushiki Kaisha | Method of manufacturing molded wooden product |
US4851458A (en) | 1986-09-11 | 1989-07-25 | Rehau Ag & Co. | Use of cellulose fibers for structurally modifying polyvinyl chloride articles |
US4810445A (en) | 1986-09-26 | 1989-03-07 | Fortifiber Corporation | Process for making pressboard from poly-coated paper |
US4769109A (en) | 1986-12-22 | 1988-09-06 | Tarkett Inc. | Relatively inexpensive thermoformable mat and rigid laminate formed therefrom |
US4769274A (en) | 1986-12-22 | 1988-09-06 | Tarkett Inc. | Relatively inexpensive thermoformable mat of reduced density and rigid laminate which incorporates the same |
US4791020A (en) | 1987-02-02 | 1988-12-13 | Novacor Chemicals Ltd. | Bonded composites of cellulose fibers polyethylene |
US4935182A (en) | 1987-02-10 | 1990-06-19 | Menzolit Gmbh | Process for producing a dimensionally stable thermoplastic semifinished product |
US4818604A (en) | 1987-03-27 | 1989-04-04 | Sub-Tank Renewal Systems, Inc. | Composite board and method |
US5028266A (en) | 1987-05-01 | 1991-07-02 | Stephan Rettenmaier | Fiber-filled granules |
US4746688A (en) | 1987-05-21 | 1988-05-24 | Ford Motor Company | Remoldable, wood-filled acoustic sheet |
US4915764A (en) | 1987-05-23 | 1990-04-10 | Mario Miani | Method of making panels |
US4874095A (en) | 1987-06-03 | 1989-10-17 | Signode System Gmbh | Edge protector and method of making same |
US4894192A (en) | 1987-08-05 | 1990-01-16 | Hans Warych | Process for producing molded bodies from paper and a thermoplastic material |
US4968463A (en) | 1987-11-06 | 1990-11-06 | Otvd (Omnium De Traitements Et De Valorisation Des Dechets) | Process for making molded or extruded objects from waste containing plastic materials |
US4988478A (en) | 1987-12-16 | 1991-01-29 | Kurt Held | Process for fabricating processed wood material panels |
US5087400A (en) | 1988-01-13 | 1992-02-11 | Wogegal S.A. | Process for making a product serving as a cultivation support |
EP0330729A1 (en) | 1988-03-03 | 1989-09-06 | Am International Incorporated | Rotary knife paper trimmer with long life shearing surfaces for trimming thick and shingled paper products |
US5183837A (en) | 1988-03-30 | 1993-02-02 | Presidenza Del Consiglio Dei Ministri - Ufficio Del Ministro Per Il Coordinamento Delle Iniziativae Per La Ricerca Scientifica E Tecnologica | Process for binding cellulosic materials with a binding agent of an aqueous emulsions of polyisocyanates and cellulose ether |
US4927579A (en) | 1988-04-08 | 1990-05-22 | The Dow Chemical Company | Method for making fiber-reinforced plastics |
US5155147A (en) | 1988-12-08 | 1992-10-13 | Werzalit Aktiengesellschaft & Co. | Method of making a pressible mixture of lignocellulose-containing fibers and a thermoplastic material having stronger bonding between the fibers and the thermoplastic material |
US5009586A (en) | 1988-12-14 | 1991-04-23 | Pallmann Maschinenfabrik Gmbh & Co. Kg | Agglomerating apparatus for the continuous regranulation of thermoplastic wastes |
US5582682A (en) | 1988-12-28 | 1996-12-10 | Ferretti; Arthur | Process and a composition for making cellulosic composites |
AU4781190A (en) | 1989-01-09 | 1990-07-12 | Peter T. Locke | A composite board and method of producing same |
US4929498A (en) | 1989-01-31 | 1990-05-29 | James River Corporation Of Virginia | Engineered-pulp wet wiper fabric |
US5057167A (en) | 1989-02-02 | 1991-10-15 | Hermann Berstorff Maschinenbau Gmbh | Method for producing chip- and fiber-board webs of uniform thickness |
US4944734A (en) | 1989-03-09 | 1990-07-31 | Micro Vesicular Systems, Inc. | Biodegradable incontinence device with embedded granules |
US4973440A (en) | 1989-03-15 | 1990-11-27 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Method for production of fiber-reinforced thermosetting resin molding material |
US6270893B1 (en) | 1989-03-20 | 2001-08-07 | Weyerhaeuser Company | Coated fiber product with adhered super absorbent particles |
US5432000A (en) | 1989-03-20 | 1995-07-11 | Weyerhaeuser Company | Binder coated discontinuous fibers with adhered particulate materials |
US5498478A (en) | 1989-03-20 | 1996-03-12 | Weyerhaeuser Company | Polyethylene glycol as a binder material for fibers |
US5516585A (en) | 1989-03-20 | 1996-05-14 | Weyerhaeuser Company | Coated fiber product with adhered super absorbent particles |
US5093058A (en) | 1989-03-20 | 1992-03-03 | Medite Corporation | Apparatus and method of manufacturing synthetic boards |
US5120776A (en) | 1989-04-19 | 1992-06-09 | Govinda Raj | Process for chemical treatment of discontinuous cellulosic fibers and composites of polyethylene and treated fibers |
US5008310A (en) | 1989-05-15 | 1991-04-16 | Beshay Alphons D | Polymer composites based cellulose-V |
US4963603A (en) | 1989-05-24 | 1990-10-16 | Armstrong World Industries, Inc. | Composite fiberboard and process of manufacture |
US5164432A (en) | 1989-06-07 | 1992-11-17 | Solvay & Cie | Moulding compositions comprising polyolefins and cellulose fibres, process for their manufacture and objects wrought from these compositions |
US5380180A (en) | 1989-07-21 | 1995-01-10 | Fortifiber Corporation | Apparatus for making pressboard from poly-coated paper using relative movement of facing webs |
EP0409525A2 (en) | 1989-07-21 | 1991-01-23 | Fortifiber Corporation | Apparatus and method for making pressboard from poly-coated paper using relative movement of facing webs |
US5137668A (en) | 1989-07-21 | 1992-08-11 | Fortifiber Corporation | Method for making pressboard from poly-coated paper using relative movement of facing webs |
US5558933A (en) | 1989-07-24 | 1996-09-24 | Aci International Limited | Sheeting material and method of manufacturing the same |
US5075359A (en) | 1989-10-16 | 1991-12-24 | Ici Americas Inc. | Polymer additive concentrate |
US5254617A (en) | 1989-11-16 | 1993-10-19 | Mitsui Petrochemical Industries, Ltd. | Resin composition for producing a film and method for producing a film by using the same |
US5002713A (en) | 1989-12-22 | 1991-03-26 | Board Of Control Of Michigan Technological University | Method for compression molding articles from lignocellulosic materials |
US5124519A (en) | 1990-01-23 | 1992-06-23 | International Paper Company | Absorbent microwave susceptor composite and related method of manufacture |
US5064692A (en) | 1990-02-15 | 1991-11-12 | International Paper Company | Method for producing paper products having increased gloss in which surface characteristics of a release film are imparted to coated substrates |
US5088910A (en) | 1990-03-14 | 1992-02-18 | Advanced Environmental Recycling Technologies, Inc. | System for making synthetic wood products from recycled materials |
US5759680A (en) | 1990-03-14 | 1998-06-02 | Advanced Environmetal Recycling Technologies, Inc. | Extruded composite profile |
US5213021A (en) | 1990-03-14 | 1993-05-25 | Advanced Environmental Recycling Technologies, Inc. | Reciprocating cutter assembly |
US5082605A (en) | 1990-03-14 | 1992-01-21 | Advanced Environmental Recycling Technologies, Inc. | Method for making composite material |
US5096406A (en) | 1990-03-14 | 1992-03-17 | Advanced Environmental Recycling Technologies, Inc. | Extruder assembly for composite materials |
US5084135A (en) | 1990-03-27 | 1992-01-28 | Advanced Environmental Recycling Technologies, Inc. | Recycling plastic coated paper product waste |
US5268074A (en) | 1990-03-27 | 1993-12-07 | Advanced Environmental Recycling Technologies, Inc. | Method for recycling polymeric film |
US5277758A (en) | 1990-03-27 | 1994-01-11 | Advanced Environmental Recycling Technologies, Inc. | Method for recycling plastic coated paper product waste and polymeric film |
US5351895A (en) | 1990-03-27 | 1994-10-04 | Advanced Environmental Recycling Technologies, Inc. | Separating device for cellulosic and thin plastic materials |
US5100603A (en) | 1990-04-30 | 1992-03-31 | Neefe Charles W | Method of recycling multimaterial containers |
US5102055A (en) | 1990-05-23 | 1992-04-07 | Didier-Werke Ag | Apparatus and process for disintegrating a fiber agglomerate |
US5134023A (en) | 1990-07-05 | 1992-07-28 | Forintek Canada Corp. | Process for making stable fiberboard from used paper and fiberboard made by such process |
WO1992007995A1 (en) | 1990-10-29 | 1992-05-14 | Tryam Trading Inc. | Treatment of absorbent sanitary paper products |
US5100545A (en) | 1990-12-03 | 1992-03-31 | Advanced Environmental Recycling Technologies, Inc. | Separation tank |
US5331087A (en) | 1990-12-29 | 1994-07-19 | Pwa Industriepapier Gmbh | Method for reprocessing thermoplast-coated packing materials and thermoplast material for further processing |
US5075057A (en) | 1991-01-08 | 1991-12-24 | Hoedl Herbert K | Manufacture of molded composite products from scrap plastics |
US5824246A (en) | 1991-03-29 | 1998-10-20 | Engineered Composites | Method of forming a thermoactive binder composite |
US5234171A (en) * | 1991-05-20 | 1993-08-10 | Cisap S.P.A. | Installation for crushing used vehicle tires and the like, and for separating the metal parts from the non-metal parts of the crushed material |
US5439542A (en) | 1991-06-14 | 1995-08-08 | Liebel; Henry L. | Composite article made from used or surplus corrugated boxes or sheets |
US5543205A (en) | 1991-06-14 | 1996-08-06 | Corrcycle, Inc. | Composite article made from used or surplus corrugated boxes or sheets |
US5366790A (en) | 1991-06-14 | 1994-11-22 | Liebel Henry L | Composite article made from used or surplus corrugated boxes or sheets |
US5194461A (en) | 1991-06-26 | 1993-03-16 | University Of Northern Iowa Foundation | Structural materials from recycled high density polyethylene and herbaceous fibers, and method for production |
US5374474A (en) | 1991-09-26 | 1994-12-20 | Earth Partners, Inc. | Composite board and method of manufacture |
US5574094A (en) | 1991-10-31 | 1996-11-12 | Montell North America Inc. | Polyolefin compositions and process for their preparation |
US5421205A (en) | 1992-02-14 | 1995-06-06 | Carl Schenck Ag | Apparatus for the rapid ultimate material strength testing of test samples |
US5372878A (en) | 1992-06-23 | 1994-12-13 | Yamasa Momi Kikaku Co., Ltd. | Slackened or creased fibrous sheet |
US5285973A (en) | 1992-07-15 | 1994-02-15 | Advanced Environmental Recycling Technologies, Inc. | Close tolerance shredder |
US5614570A (en) | 1992-08-17 | 1997-03-25 | Weyerhaeuser Company | Absorbent articles containing binder carrying high bulk fibers |
US5571618A (en) | 1992-08-17 | 1996-11-05 | Weyerhaeuser Company | Reactivatable binders for binding particles to fibers |
US5547745A (en) | 1992-08-17 | 1996-08-20 | Weyerhaeuser Company | Particle binders |
US6425979B1 (en) | 1992-08-17 | 2002-07-30 | Weyerhaeuser Company | Method for making superabsorbent containing diapers |
US6521087B2 (en) | 1992-08-17 | 2003-02-18 | Weyerhaeuser Company | Method for forming a diaper |
US6015611A (en) | 1992-08-31 | 2000-01-18 | Andersen Corporation | Advanced polymer wood composite |
US5773138A (en) | 1992-08-31 | 1998-06-30 | Andersen Corporation | Advanced compatible polymer wood fiber composite |
US5539027A (en) | 1992-08-31 | 1996-07-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US6015612A (en) | 1992-08-31 | 2000-01-18 | Andersen Corporation | Polymer wood composite |
US5932334A (en) | 1992-08-31 | 1999-08-03 | Andersen Corporation | Advanced polymer wood composite |
US6004668A (en) | 1992-08-31 | 1999-12-21 | Andersen Corporation | Advanced polymer wood composite |
US5486553A (en) | 1992-08-31 | 1996-01-23 | Andersen Corporation | Advanced polymer/wood composite structural member |
US5981067A (en) | 1992-08-31 | 1999-11-09 | Andersen Corporation | Advanced compatible polymer wood fiber composite |
US5827607A (en) | 1992-08-31 | 1998-10-27 | Andersen Corporation | Advanced polymer wood composite |
US6210792B1 (en) | 1992-08-31 | 2001-04-03 | Andersen Corporation | Advanced compatible polymer wood fiber composite |
US5985429A (en) | 1992-08-31 | 1999-11-16 | Andersen Corporation | Polymer fiber composite with mechanical properties enhanced by particle size distribution |
US5497594A (en) | 1992-09-01 | 1996-03-12 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5406768A (en) | 1992-09-01 | 1995-04-18 | Andersen Corporation | Advanced polymer and wood fiber composite structural component |
US5298102A (en) | 1993-01-08 | 1994-03-29 | Sorbilite Inc. | Expanding pressure chamber for bonding skins to flat and shaped articles |
US5284610A (en) | 1993-02-09 | 1994-02-08 | Kang Na Hsiung Enterprise Co., Ltd. | High molecular absorbent sheet manufacturing process and the related equipment |
US5441801A (en) | 1993-02-12 | 1995-08-15 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5518677A (en) | 1993-02-12 | 1996-05-21 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5695874A (en) | 1993-02-12 | 1997-12-09 | Andersen Corporation | Advanced polymer/wood composite pellet process |
US5350370A (en) | 1993-04-30 | 1994-09-27 | Kimberly-Clark Corporation | High wicking liquid absorbent composite |
US5767177A (en) | 1993-05-04 | 1998-06-16 | Cytec Industry Incorporated | Injection mouldable thermosetting composition especially for motor vehicle bodies, method of production and method or recycling |
US5582847A (en) | 1993-05-28 | 1996-12-10 | Repete Corporation | Optimizing pellet mill controller |
US5618858A (en) | 1993-07-05 | 1997-04-08 | Siemens Aktiengesellschaft | Polymer material |
US5663216A (en) | 1993-07-28 | 1997-09-02 | Bio-Tec Biologische Naturverpackungen Gmbh | Reinforced biodegradable polymer |
DE4331747A1 (en) | 1993-09-20 | 1995-03-23 | Wuenning Paul | Extruded, fiber-reinforced natural material granulate for thermoplastic processing, and process for its production |
US5416139A (en) | 1993-10-07 | 1995-05-16 | Zeiszler; Dennis E. | Structural building materials or articles obtained from crop plants or residues therefrom and/or polyolefin materials |
US5682015A (en) | 1993-10-15 | 1997-10-28 | Georgia Power Company | Squirrel shield device |
US5437766A (en) | 1993-10-22 | 1995-08-01 | The Procter & Gamble Company | Multi-ply facial tissue paper product comprising biodegradable chemical softening compositions and binder materials |
US5516472A (en) | 1993-11-12 | 1996-05-14 | Strandex Corporation | Extruded synthetic wood composition and method for making same |
US5540244A (en) | 1993-12-07 | 1996-07-30 | Advanced Environmental Recycling Technologies, Inc. | Method and apparatus for cleaning and recycling post-consumer plastic films |
US5791262A (en) | 1994-02-14 | 1998-08-11 | The Fabri-Form Co. | Reinforced plastic pallet |
US5643635A (en) | 1994-02-16 | 1997-07-01 | Chan-Hee Shin | Method and composition for forming a decorative coating on a substrate |
US5480602A (en) | 1994-06-17 | 1996-01-02 | Nagaich; Laxmi | Extruded particle board |
US5439749A (en) | 1994-08-18 | 1995-08-08 | Andersen Corporation | Composite wood structure |
US5585150A (en) | 1994-09-08 | 1996-12-17 | Mulch Developement Company | Mulch product and process for its preparation |
US5746958A (en) | 1995-03-30 | 1998-05-05 | Trex Company, L.L.C. | Method of producing a wood-thermoplastic composite material |
US6106944A (en) | 1995-06-07 | 2000-08-22 | Andersen Corporation | Fiber thermoset reinforced thermoplastic structural member |
US5585155A (en) | 1995-06-07 | 1996-12-17 | Andersen Corporation | Fiber reinforced thermoplastic structural member |
US6007656A (en) | 1995-06-07 | 1999-12-28 | Andersen Corporation | Fiber reinforced thermoplastic structural member |
US5876641A (en) | 1995-07-31 | 1999-03-02 | Andersen Corporation | In-line process for injection of foam material into a composite profile |
US5643359A (en) | 1995-11-15 | 1997-07-01 | Dpd, Inc. | Dispersion of plant pulp in concrete and use thereof |
US5851469A (en) | 1995-12-27 | 1998-12-22 | Trex Company, L.L.C. | Process for making a wood-thermoplastic composite |
US5948524A (en) | 1996-01-08 | 1999-09-07 | Andersen Corporation | Advanced engineering resin and wood fiber composite |
US5819491A (en) | 1996-01-22 | 1998-10-13 | L.B. Plastics Limited | Modular construction elements |
EP0801168A1 (en) | 1996-04-09 | 1997-10-15 | Ein Engineering Co., Ltd. | Method and apparatus for recycling laminated film |
US20030207064A1 (en) | 1996-04-29 | 2003-11-06 | Bunyan Michael H. | Conformal thermal interface material for electronic components |
US5882564A (en) | 1996-06-24 | 1999-03-16 | Andersen Corporation | Resin and wood fiber composite profile extrusion method |
US20040005461A1 (en) | 1996-07-11 | 2004-01-08 | Nagle Dennis C. | Carbonized wood-based materials |
US6085923A (en) | 1996-08-13 | 2000-07-11 | Neocork Technologies, Inc. | Composite synthetic stopper |
US6117924A (en) | 1996-10-22 | 2000-09-12 | Crane Plastics Company Limited Partnership | Extrusion of synthetic wood material |
US6180257B1 (en) | 1996-10-29 | 2001-01-30 | Crane Plastics Company Limited Partnership | Compression molding of synthetic wood material |
US6511757B1 (en) | 1996-10-29 | 2003-01-28 | Crane Plastics Company Llc | Compression molding of synthetic wood material |
US6200682B1 (en) | 1996-12-11 | 2001-03-13 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials and products made by the method |
US6821614B1 (en) | 1996-12-11 | 2004-11-23 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials, and products made by the method |
US6357197B1 (en) | 1997-02-05 | 2002-03-19 | Andersen Corporation | Polymer covered advanced polymer/wood composite structural member |
US6346160B1 (en) | 1997-03-28 | 2002-02-12 | Andersen Corporation | Thermoplastic resin and fiberglass fabric composite and method |
US5948505A (en) | 1997-03-28 | 1999-09-07 | Andersen Corporation | Thermoplastic resin and fiberglass fabric composite and method |
US6969781B2 (en) | 1997-05-13 | 2005-11-29 | Weyeerhaeuser Company | Reticulated absorbent composite |
US6122877A (en) | 1997-05-30 | 2000-09-26 | Andersen Corporation | Fiber-polymeric composite siding unit and method of manufacture |
US5952105A (en) | 1997-09-02 | 1999-09-14 | Xyleco, Inc. | Poly-coated paper composites |
US6448307B1 (en) | 1997-09-02 | 2002-09-10 | Xyleco, Inc. | Compositions of texturized fibrous materials |
EP1015242B1 (en) | 1997-09-02 | 2006-04-05 | Xyleco, Inc. | Poly-coated paper composites |
US20030032702A1 (en) | 1997-09-02 | 2003-02-13 | Marshall Medoff | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US20060240109A1 (en) | 1997-09-02 | 2006-10-26 | Xyleco, Inc., A Massachusetts Corporation | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US20030187102A1 (en) | 1997-09-02 | 2003-10-02 | Marshall Medoff | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US20020010229A1 (en) | 1997-09-02 | 2002-01-24 | Marshall Medoff | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US20050080168A1 (en) | 1997-09-02 | 2005-04-14 | Xyleco, Inc., A Massachusetts Corporation | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6685858B2 (en) | 1997-09-05 | 2004-02-03 | Crane Plastics Company Llc | In-line compounding and extrusion system |
US5973035A (en) | 1997-10-31 | 1999-10-26 | Xyleco, Inc. | Cellulosic fiber composites |
US6258876B1 (en) | 1997-10-31 | 2001-07-10 | Xyleco, Inc. | Cellulosic fiber composites |
US6207729B1 (en) | 1997-10-31 | 2001-03-27 | Xyleco, Inc. | Texturized cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6605245B1 (en) | 1997-12-11 | 2003-08-12 | Boise Cascade Corporation | Apparatus and method for continuous formation of composites having filler and thermoactive materials |
US5871162A (en) * | 1998-01-02 | 1999-02-16 | Robert C. Rajewski | Paper shredding assembly |
US6029916A (en) * | 1998-01-16 | 2000-02-29 | Terra Technologies, Inc. | System and method for decomposing reclaiming and refusing waste carpet materials |
US6054207A (en) | 1998-01-21 | 2000-04-25 | Andersen Corporation | Foamed thermoplastic polymer and wood fiber profile and member |
US6344268B1 (en) | 1998-04-03 | 2002-02-05 | Certainteed Corporation | Foamed polymer-fiber composite |
US6284098B1 (en) | 1998-07-20 | 2001-09-04 | Wwj, Llc | Lignocellulose fiber filler for thermoplastic composite compositions |
US6270883B1 (en) | 1998-10-09 | 2001-08-07 | The United States Of America As Represented By The Secretary Of Agriculture | Composites containing cellulosic pulp fibers and methods of making and using the same |
US6730249B2 (en) | 1998-10-09 | 2004-05-04 | The United States Of America As Represented By The Secretary Of Agriculture | Methods of making composites containing cellulosic pulp fibers |
US6409952B1 (en) | 1998-11-25 | 2002-06-25 | Crane Plastics Company Limited Partnership | Drying and processing cellulosic compounds |
US6495225B1 (en) | 1998-12-25 | 2002-12-17 | Konica Corporation | Molding material |
US6337138B1 (en) | 1998-12-28 | 2002-01-08 | Crane Plastics Company Limited Partnership | Cellulosic, inorganic-filled plastic composite |
US6479002B1 (en) | 1998-12-30 | 2002-11-12 | Haller Formholz | Extrusion of plant materials encapsulated in a thermoplastic |
US6265037B1 (en) | 1999-04-16 | 2001-07-24 | Andersen Corporation | Polyolefin wood fiber composite |
US6682789B2 (en) | 1999-04-16 | 2004-01-27 | Andersen Corporation | Polyolefin wood fiber composite |
US6680090B2 (en) | 1999-04-16 | 2004-01-20 | Andersen Corporation | Polyolefin wood fiber composite |
US6420626B1 (en) | 1999-06-08 | 2002-07-16 | Buckeye Technologies Inc. | Unitary fluid acquisition, storage, and wicking material |
US20060247336A1 (en) | 1999-06-22 | 2006-11-02 | Xyleco, Inc., A Massachusetts Corporation | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US20070015855A1 (en) | 1999-06-22 | 2007-01-18 | Xyleco, Inc., A Massachusetts Corporation | Cellulosic and lignocellulosic materials and compositions and composites made therefrom |
WO2000078127A1 (en) | 1999-06-22 | 2000-12-28 | Xyleco, Inc. | Texturized cellulosic and lignocellulosic materials and compositions and composites made therefrom |
EP1207740B1 (en) | 1999-06-22 | 2006-12-06 | Xyleco, Inc. | Texturized cellulosic and lignocellulosic materials and compositions and composites made therefrom |
US6784230B1 (en) | 1999-09-23 | 2004-08-31 | Rohm And Haas Company | Chlorinated vinyl resin/cellulosic blends: compositions, processes, composites, and articles therefrom |
US6746976B1 (en) | 1999-09-24 | 2004-06-08 | The Procter & Gamble Company | Thin until wet structures for acquiring aqueous fluids |
US20020019614A1 (en) | 2000-05-17 | 2002-02-14 | Woon Paul S. | Absorbent articles having improved performance |
US20050200050A1 (en) | 2000-06-13 | 2005-09-15 | Xyleco Inc., | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US6620503B2 (en) | 2000-07-26 | 2003-09-16 | Kimberly-Clark Worldwide, Inc. | Synthetic fiber nonwoven web and method |
US6692825B2 (en) | 2000-07-26 | 2004-02-17 | Kimberly-Clark Worldwide, Inc. | Synthetic fiber nonwoven web and method |
US6824729B2 (en) | 2000-07-26 | 2004-11-30 | Kimberly-Clark Worldwide, Inc. | Process of making a nonwoven web |
WO2002014039A1 (en) | 2000-08-10 | 2002-02-21 | California Agriboard, Llc. | Production of particle board from agricultural waste |
US6638612B2 (en) | 2000-09-18 | 2003-10-28 | James D. Jones | Thermoplastic composite wood material |
US6322664B1 (en) * | 2000-10-17 | 2001-11-27 | Voith Sulzer Paper Technology North America, Inc. | Method of processing recycled waste paper by separating fibers of different colors |
US6617376B2 (en) | 2001-03-30 | 2003-09-09 | Crane Plastics Company Llc | Flexible wood composition |
US20030100634A1 (en) | 2001-04-16 | 2003-05-29 | Heath Richard B. | Composite compositions |
US20040140069A1 (en) * | 2001-04-23 | 2004-07-22 | Roland Selin | Production of fiber suspension from waste paper |
US20030021915A1 (en) | 2001-06-15 | 2003-01-30 | Vivek Rohatgi | Cellulose - polymer composites and related manufacturing methods |
US6758996B2 (en) | 2001-07-13 | 2004-07-06 | Kadant Composites Inc. | Cellulose-reinforced thermoplastic composite and methods of making same |
US6632863B2 (en) | 2001-10-25 | 2003-10-14 | Crane Plastics Company Llc | Cellulose/polyolefin composite pellet |
US20030121380A1 (en) | 2001-11-30 | 2003-07-03 | Cowell Christine M. | System for aperturing and coaperturing webs and web assemblies |
US20030125688A1 (en) | 2001-11-30 | 2003-07-03 | Keane James M. | Adhesive system for mechanically post-treated absorbent structures |
US6780359B1 (en) | 2002-01-29 | 2004-08-24 | Crane Plastics Company Llc | Synthetic wood composite material and method for molding |
WO2003079763A1 (en) | 2002-03-21 | 2003-10-02 | Xyleco, Inc. | Compositions and composites of cellulosic and lignocellulosic materials and resins, and methods of making the same |
US6670035B2 (en) | 2002-04-05 | 2003-12-30 | Arteva North America S.A.R.L. | Binder fiber and nonwoven web |
US6743507B2 (en) | 2002-06-07 | 2004-06-01 | Rayonier Products And Financial Services Company | Cellulose fiber reinforced composites having reduced discoloration and improved dispersion and associated methods of manufacture |
US6855182B2 (en) | 2002-07-17 | 2005-02-15 | Rayonier Products And Financial Services Company | Lignocellulose fiber composite with soil conditioners |
US20040072924A1 (en) | 2002-10-09 | 2004-04-15 | Crompton Corporation | Natural fiber-filled polyolefin composites |
US7708214B2 (en) * | 2005-08-24 | 2010-05-04 | Xyleco, Inc. | Fibrous materials and composites |
Non-Patent Citations (20)
Title |
---|
Abstract of (Doctorate) Dissertation Abstract Int. B1988, 58(9), 4962 (published in Sep. 1997), in Chemical Abstracts 128:128805. |
Abstract of JP 09213296, filed Feb. 5, 1996, in Chemical Abstracts 127:223004. |
Abstract of JP 09267441, filed Oct. 14, 1997, in Chemical Abstracts 127:294599. |
Communication Pursuant to Article 94(3) EPC for EP Application No. 06739443.7-2307/1877192 (PCT/US2006/010648), mailed Jun. 15, 2010, 7 pages. |
Dalvag et al., "The Efficiency of Cellulosic Fillers in Common Thermoplastics. Part II. Filling with Process Aids and Coupling Agents", International Journal of Polymeric Materials, 1985, vol. 11, pp. 9-38. |
ESR for EP Application No. 06739443.7-2307/1877192 (PCT/US2006/010648), mailed Mar. 3, 2010, 11 pages. |
Klason et al., "The Efficiency of Cellulosic Fillers in Common Thermoplastics. Part I. Filling Without Processing Aids or Coupling Agents", International Journal of Polymeric Materials, Mar. 1984, pp. 159-187. |
Kokta et al., "Composites of Poly(Vinyl Chloride) and Wood Fibers. Part II: Effect of Chemical Treatment", Polymer Composites, Apr. 1990, vol. 11, No. 2, pp. 84-89. |
Kokta et al., "Composites of Polyvinyl Chloride-Wood Fibers. I. Effect of Isocyanate as a Bonding Agent", Polym. Plast. Technol. Eng. 29(1&2), 1990, pp. 87-118. |
Kokta et al., "Composites of Polyvinyl Chloride-Wood Fibers. III. Effect of Silane as Coupling Agent", Journal of Vinyl Technology, Sep. 1990, vol. 12, No. 3, pp. 146-153. |
Kokta et al., "Use of Grafted Wood Fibers in Thermoplastic Composites V. Polystyrene", pp. 85-96. |
Kokta et al., "Use of Wood Fibers in Thermoplastic Composites", Polymer Composites, Oct. 1983, vol. 4, No. 4, pp. 229-232. |
Maldas et al., "Composites of Polyvinyl Chloride-Wood Fibers: IV. Effect of the Nature of Fibers", Journal of Vinyl Technology, Jun. 1989, vol. 11, No. 2, pp. 90-98. |
Raj et al., "Use of Wood Fibers as Filler in Common Thermoplastic Studies on Mechanical Properties", Science and Engineering of Composite Materials, vol. 1, No. 3, 1989, pp. 85-98. |
Raj et al., "Use of Wood Fibers in Thermoplastics. VII. The Effect of Coupling Agents in Polyethylene-Wood Fiber Composites", Journal of Applied Polymer Science, vol. 37, (1989), pp. 1089-1103. |
Rogalski et al., "Poly(Vinyl-Chloride) Wood Fiber Composites", Antec '87, pp. 1436-1441. |
Supplementary European Search Report, EP 03 71 1572, Feb. 28, 2005. |
Woodhams et al., "Wood Fibers as Reinforcing Fillers for Polyolefins", Polymer Engineering and Science, Oct. 1984, vol. 24, No. 15, pp. 1166-1171. |
Yam et al., "Composites From Compounding Wood Fibers With Recycled High Density Polyethylene", Polymer Engineering and Science, Mid-Jun. 1990, vol. 30, No. 11, pp. 693-699. |
Zadorecki et al., "Future Prospects for Wood Cellulose as Reinforcement in Organic Polymer Composites", Polymer Composites, Apr. 1989, vol. 10, No. 2, pp. 69-77. |
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